Heat buffer and storage

Scout intake sheet

3
Challenge description

Within the heat integration cluster of the Institute for Sustainable Process Technology (ISPT), the foundation is laid for a nationally supported cross-sectoral Integrated Circular Heat Program, in which innovation and practice are actively linked. Indeed, for a large number of companies in the agro-food, paper, chemical, horticultural and food sectors, heat is the biggest energy consumer. Therefore, heat technologies need to be vastly integrated to reach a carbon neutral heat supply for all temperature levels by 2050. As this knowledge is spread through various industries and discipline, ISPT wants to present to its partners an overview of the existing technologies that are linked with the (re-)use and storage of heat. This specific scouting case will focus on heat storage and heat buffers. These technologies can have different storage timescales (seasonal or daily). Of interest are the capacity, the efficiency, the flow rate, the temperatures, the size and the TRL. The search should focus on integrated and applied systems (i.e. no lab searches on materials) that either have a low energy output, but many possible applications (as district or domestic heat use) or a high energy output but for a small number of applications (as industrial). However, if the scope is too large, the focus should be set on industrial systems. 

Scope
Discover Demonstrate Develop Deploy
Current known technique(s)
  • Sensible heat storage
  • Latent heat storage (ex: phase change materials)
  • Thermochemical heat storage
Ideal outcome

An overview of all the existing methods for storing heat with their specification and suppliers

Minimum viable outcome

A list of all the existing systems to store heat

Objective(s)
  • Capacity/Timeframe
  • Duration / Timescale
  • Size
  • Efficiency
  • Temperature
Constraint(s)
  • Complete system (not a fundamental material in a lab)
  • Density
Functions
Action = [store] OR [store] OR [reuse]

Object = [heat] OR [energy] OR [heat]

Environment = [Residential] OR [Industrial] OR [thermal energy storage] OR [heat] OR [pilot] OR [heat] OR [waste heat] OR [storage] OR [latent] OR [phase change material] OR [water] OR [sensible] OR [solid] OR [PCM] OR [liquid] OR [thermochemical] OR [solid solid] OR [concrete] OR [heat pipe] OR [cavern] OR [sand] OR [heat] OR [storage] OR [oils] OR [thermal] OR [solar cookers] OR [salt] OR [concrete] OR [PCM] OR [high temperature] OR [metal foam] OR [adsorption]
Terminology
  • PCM (Phase Change Materials)
Case Confirmation
Confirmed by

Preliminary Results

Concept Technology Selection
1. Solid sensible heat storage (S-SHS)
Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on solid materials
1.1 Concrete storage pile

0 of 0
1.2 Granular materials (Sand and rocks)

0 of 0
1.3 Natural Rock/cavern storage

0 of 0
1.4 Sand

0 of 0
1.5 Solid industrial waste byproduct

0 of 0
2. Liquid sensible heat storage (L-SHS)
Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on liquids
2.1 Aquifer Thermal Energy Storage (ATES)

0 of 0
2.2 Thermally (Vacuum) insulated water tank

0 of 0
2.3 Oils

0 of 0
2.4 Molten Salts

0 of 0
2.5 Aqueous calcium chloride

0 of 0
2.6 Heat and ground pumped hydro energy storage

0 of 0
2.7 Ammonium - water storage tanks

0 of 0
3. Mix of solid - liquid sensible heat (SL-SHS)
Mix of liquid and solid heat storage
3.1 Borehole thermal energy storage (Soil storage)

0 of 0
4. Solid-solid latent heat storage (SS-LHS)
Solid-solid phase change materials(SS-PCMs) absorb andrelease heat by reversible phase transitions between a (solid) crys-talline or semi-crystalline phase, and another (solid) amorphous,semi-crystalline, or crystalline phase. Different from solid-liquid-PCMs, solid-solid-PCMs retain their bulk solid properties withincertain temperature ranges and are therefore also referred to as ‘‘solid-state” PCMs
4.1 Inorganic

0 of 0
4.2 Organic

0 of 0
4.3 Organo-Metallic

0 of 0
4.4 Polymeric

0 of 0
5. Solid-liquid latent heat storage (SL-LHS)
Generally, LHS systems use the latent heat between solid andliquid phases of the storage medium, whereby the PCM is requiredto be contained or encapsulated within a container to prevent theliquid from leaking; however, the capsules decrease the energydensity of the system and increase the cost of production. Such storage has potential in heating and cooling buildings, waste heat recovery, offpeak power utilization, heat pump systems, tanks and many other applications
5.1 Non-parafins (Organic)

0 of 0
5.2 Parafin (Organic)

0 of 0
5.3 Metallic alloys (Inorganic)

0 of 0
5.4 Salt Hydrates and compositions (Inorganic)

0 of 0
5.5 Eutetic phase change materials

0 of 0
5.6 Alkanes

0 of 0
5.7 Fine powdered composite for latent heat storage [R]

0 of 0
5.8 Ice/Water Heat pipe for cold storage

0 of 0
5.9 Heat Pipes

0 of 0
6. Latent Integration technologies
Technolgies to integrate Phase Change Materials into processes.
6.1 Building materials filled with PCM

0 of 0
6.2 Phase Change Material in water tanks

0 of 0
6.3 Bed Storage concept

0 of 0
6.4 Heat exchanger integration

0 of 0
6.5 High temperature concrete as storage media

0 of 0
6.6 Micro encapsulated PCM

0 of 0
6.7 Nano PCM

0 of 0
6.8 Supercooling

0 of 0
6.9 Adsorption pump

0 of 0
6.10 Steam integration

0 of 0
6.11 Heat pipes filled with PCM

0 of 0
6.12 Supercritical fluids with PCM

0 of 0
6.13 Metal foams

0 of 0
7. Thermochemical heat storage (THS)
THS systems can utilise both sorption and chemical reactions to generate heat and in order to achieve efficient and economically acceptable systems, the appropriate reversible reactions (suitable to the user demand needs) need to be identified
7.1 Hydroxides (M(OH)2)

0 of 0
7.2 Metal Carbonates (MCO3)

0 of 0
7.3 Metal sulfates (MSO4)

0 of 0
7.4 Pure metal oxides (MO)

0 of 0
7.5 Zeolite

0 of 0
7.6 Silica Gel

0 of 0
7.7 Zeo-like Materials

0 of 0
7.8 Composite

0 of 0
7.9 Metal Hydrides

0 of 0

Published 07/28/2019

Based on the case described above we have executed the first line of queries in IGOR^AI. The goal was to obtain a broad set of techniques that store heat. Thermal Energy Storage systems can be classified according to different parameters, being the temperature range of application, the mechanism of energy storage, and the integration within the energy storage concept. As the later can be really broad, it has been chosen to separate the concepts on the mechanism of energy storage and from there on derive later temperature range. Example of storage concepts are shown for PCM materials as both materials and integration process are important. 7 concepts are distinguished based on the results: 1. Solid sensible heat storage (S-SHS) 2. Liquid sensible heat storage (L-SHS) 3. Mix of solid - liquid sensible heat (SL-SHS) 4. Solid-solid latent heat storag (SS-LHS) 5. Solid-liquid latent heat storage (SL-LHS) 6. Latent Integration technologies 7. Thermochemical heat storage (THS) Every concept comprises multiple techniques (49 in total). Below the table, short descriptions, research findings and sources per techniques are listed as well. You can use this information to get a better understanding of the techniques. During the midway meeting, we would like to discuss the techniques and concepts, determine their relevance and select the top selection that needs to be deepened in the second phase of the project.

To determine which technologies are relevant to proceed to the next scouting phase you can play the technology selection game by clicking on the button below.

Concept Technology Selection
1. Solid sensible heat storage (S-SHS)
Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on solid materials
1.1 Concrete storage pile

0 of 0
1.2 Granular materials (Sand and rocks)

0 of 0
1.3 Natural Rock/cavern storage

0 of 0
1.4 Sand

0 of 0
1.5 Solid industrial waste byproduct

0 of 0
2. Liquid sensible heat storage (L-SHS)
Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on liquids
2.1 Aquifer Thermal Energy Storage (ATES)

0 of 0
2.2 Thermally (Vacuum) insulated water tank

0 of 0
2.3 Oils

0 of 0
2.4 Molten Salts

0 of 0
2.5 Aqueous calcium chloride

0 of 0
2.6 Heat and ground pumped hydro energy storage

0 of 0
2.7 Ammonium - water storage tanks

0 of 0
3. Mix of solid - liquid sensible heat (SL-SHS)
Mix of liquid and solid heat storage
3.1 Borehole thermal energy storage (Soil storage)

0 of 0
4. Solid-solid latent heat storage (SS-LHS)
Solid-solid phase change materials(SS-PCMs) absorb andrelease heat by reversible phase transitions between a (solid) crys-talline or semi-crystalline phase, and another (solid) amorphous,semi-crystalline, or crystalline phase. Different from solid-liquid-PCMs, solid-solid-PCMs retain their bulk solid properties withincertain temperature ranges and are therefore also referred to as ‘‘solid-state” PCMs
4.1 Inorganic

0 of 0
4.2 Organic

0 of 0
4.3 Organo-Metallic

0 of 0
4.4 Polymeric

0 of 0
5. Solid-liquid latent heat storage (SL-LHS)
Generally, LHS systems use the latent heat between solid andliquid phases of the storage medium, whereby the PCM is requiredto be contained or encapsulated within a container to prevent theliquid from leaking; however, the capsules decrease the energydensity of the system and increase the cost of production. Such storage has potential in heating and cooling buildings, waste heat recovery, offpeak power utilization, heat pump systems, tanks and many other applications
5.1 Non-parafins (Organic)

0 of 0
5.2 Parafin (Organic)

0 of 0
5.3 Metallic alloys (Inorganic)

0 of 0
5.4 Salt Hydrates and compositions (Inorganic)

0 of 0
5.5 Eutetic phase change materials

0 of 0
5.6 Alkanes

0 of 0
5.7 Fine powdered composite for latent heat storage [R]

0 of 0
5.8 Ice/Water Heat pipe for cold storage

0 of 0
5.9 Heat Pipes

0 of 0
6. Latent Integration technologies
Technolgies to integrate Phase Change Materials into processes.
6.1 Building materials filled with PCM

0 of 0
6.2 Phase Change Material in water tanks

0 of 0
6.3 Bed Storage concept

0 of 0
6.4 Heat exchanger integration

0 of 0
6.5 High temperature concrete as storage media

0 of 0
6.6 Micro encapsulated PCM

0 of 0
6.7 Nano PCM

0 of 0
6.8 Supercooling

0 of 0
6.9 Adsorption pump

0 of 0
6.10 Steam integration

0 of 0
6.11 Heat pipes filled with PCM

0 of 0
6.12 Supercritical fluids with PCM

0 of 0
6.13 Metal foams

0 of 0
7. Thermochemical heat storage (THS)
THS systems can utilise both sorption and chemical reactions to generate heat and in order to achieve efficient and economically acceptable systems, the appropriate reversible reactions (suitable to the user demand needs) need to be identified
7.1 Hydroxides (M(OH)2)

0 of 0
7.2 Metal Carbonates (MCO3)

0 of 0
7.3 Metal sulfates (MSO4)

0 of 0
7.4 Pure metal oxides (MO)

0 of 0
7.5 Zeolite

0 of 0
7.6 Silica Gel

0 of 0
7.7 Zeo-like Materials

0 of 0
7.8 Composite

0 of 0
7.9 Metal Hydrides

0 of 0

1. Solid sensible heat storage (S-SHS)

Back

Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on solid materials


1.1 Concrete storage pile

0

The use of concrete geostructures for energy extraction and storage in the ground is an environmentally friendly and easy way of cooling and heating buildings. With such energy geostructures, it is possible to transfer energy from the ground to buildings by means of fluid-filled pipes cast in concrete. By injecting thermal energy in summer and extracting it in winter, the ground in the area of a building’s piles can be used for seasonal energy storage, as long as the underground water flow in the storage remains low. Most buildings use piles for the foundation, and these piles can easily contain heat exchangers in contact with the soil. The so-called ‘energy pile’ can thus fulfil a double function: foundation plus heat exchange. Heat pumps can then transfer heat very efficiently from the ground to be building interior and vice-versa. Heat exchange with the ground can be via thermoactive foundations. In thermoactive foundations, foundation piles, also referred to as "thermal piles" or as "energy piles", are used as heat exchangers for supplying low temperature heat to heat pumps. They can also be used for underground storage of warmth supplied by road solar collectors. Some suppliers also propose heat storage in concrete piles as a flexible installation that is not used as a building foundation and can be used as an add on to an existing building or district (see Energy Nest).

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1.2 Granular materials (Sand and rocks)

0

Granular materials such as sand and rocks are studied to present an additional HTF to represent an efficient and costeffective alternative. Low cost solid particulates can store and transport heat at temperatures over 1000°C. **_Examples:_** - Dead Sea salt, concrete bed and Basalt rocks are more economically attractive relative to molten salt plant because they eliminate the extra cost associated with freeze protection, no pressurizing problem, no corrosion. Finally, natural stones can operate at higher temperature and do not suffer from cracking due to cyclic charging and discharging. - For the purpose of heat recovery, a moving bed heat exchanger (MBHX) is applied and tested. In this study, the dense granular mass is gravitydriven through a heat exchanger. The performance of the MBHX with the utilization of Sand, Basalt, and a Mixture of Sand and Basalt as a granular material was experimentally investigated. It is found that the effectiveness of the MBHX using a mixture of 50% sand and 50% basalt improved by 30% compared to using sand alone.

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1.3 Natural Rock/cavern storage

0

TES system using underground rock carven is considered as an attractive alternative for largescale storage, because of low thermal conductivity and chemical safety of surrounding rock mass. Based on some successful applications of cavern storage and hightemperature storage reported in the literature, the applicabilities and practicabilities of storage media and technologies for largescale cavern thermal energy storage (CTES) were reviewed Ex: Basalt rocks

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1.4 Sand

0

Seasonal sandbed solar thermal storage systems are an excellent option for storing heat for climates in regions with long periods of freezing temperatures. The present study shows a proof of concept of a sandbed seasonal solar thermal storage that needs additional controls for residential heating application. The system could also be used to provide heat for unoccupied spaces such as garages and greenhouses. Can also be used for solar powerplants were the intent of the receiver is to be used as a part of a sensible thermal energy storage system for concentrated solar power plants based upon the concept of storing solar heat in sand particles for a later discharge through a specific sandsteam heat exchanger. The results of the analysis indicate low efficiency figures that can be caused by imperfections on the experimental setup and on the original design. Several paths of improvement are discussed in conclusion.

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1.5 Solid industrial waste byproduct

0

Within all the properties that define the suitability of a material to store sensible heat, waste materials stand out especially for their low costs and availability. This heat recovery could be used for cogeneration, energy efficiency measures, passive heat recovery, solar cooling, etc. In this case, a solid by-product from the potash industry is tested in two different shapes to be used for industrial sensible heat recovery in high temperature, in a range of 100–200 °C. This heat recovery could be used for cogeneration, energy efficiency measures, passive heat recovery, solar cooling, etc. In this case, it is mostly made of NaCl

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2. Liquid sensible heat storage (L-SHS)

Back

Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on liquids


2.1 Aquifer Thermal Energy Storage (ATES)

0

Aquifer thermal energy storage (ATES) is the storage and recovery of thermal energy in the subsurface. ATES is applied to provide heating and cooling to buildings. Storage and recovery of thermal energy is achieved by extraction and injection of groundwater from aquifers using groundwater wells. Systems commonly operate in a seasonal mode. The groundwater that is extracted in summer, is used for cooling by transferring heat from the building to the groundwater by means of a heat exchanger. Subsequently, the heated groundwater is injected back into the aquifer, which creates a storage of heated groundwater. In wintertime, the flow direction is reversed such that the heated groundwater is extracted and can be used for heating (often in combination with a heat pump). Therefore, operating an ATES system uses the subsurface as a temporal storage to buffer seasonal variations in heating and cooling demand. When replacing traditional fossil fuel dependent heating and cooling systems, ATES can serve as a cost-effective technology to reduce the primary energy consumption of a building and the associated CO2 emissions.

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2.2 Thermally (Vacuum) insulated water tank

0

The solar heat energy is stored in a thermally insulated water tank and used in the heating period. The heat is also stored in the ground if necessary, using the ground loop of the heat pump if the water tank’s temperature rises above a certain threshold. If the temperature is too low for direct heating, then the heat pump can be used to extract the stored energy. This can also be performed under the form of a large subterranean buffer tank filled with water. Heat and cold can be added to or extracted from the tank through conductivity via its wall.

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2.3 Oils

0

Thermal oils have the advantage that they act both as the heat transfer and the heat storage medium for medium to high temperature domestic applications. These applications include steam generation and cooking of food. Although thermal oils are more expensive than water which is in abundance, the use of water in medium to high temperatures is limited by its boiling point. For small scale domestic applications which require non-sophisticated heat exchangers, thermal oils can be utilized.

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2.4 Molten Salts

0

Molten salts can be employed as a thermal energy storage method to retain thermal energy. Presently, this is a commercially used technology to store the heat collected by concentrated solar power (e.g., from a solar tower or solar trough). The heat can later be converted into superheated steam to power conventional steam turbines and generate electricity in bad weather or at night. The salt melts at 131 °C (268 °F). It is kept liquid at 288 °C (550 °F) in an insulated "cold" storage tank. The liquid salt is pumped through panels in a solar collector where the focused sun heats it to 566 °C (1,051 °F). It is then sent to a hot storage tank. With proper insulation of the tank the thermal energy can be usefully stored for up to a week.[15] When electricity is needed, the hot molten-salt is pumped to a conventional steam-generator to produce superheated steam for driving a conventional turbine/generator set as used in any coal or oil or nuclear power plant Different existing concept and salts: Two tanks / One tank storage using NaNo3/ KNO3 / Ca(NO3)2

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2.5 Aqueous calcium chloride

0

A new concept for longterm solar storage is based on the absorption properties of aqueous calcium chloride. Water, diluted and concentrated calcium chloride solutions are stored in a single tank. An immersed heat exchanger and stratification manifold are used to preserve longterm sorption storage, and to achieve thermal stratification. The feasibility of the concept is demonstrated via measurements of velocity, CaCl2 mass fraction, and temperature in a 1500 liter prototype tank during sensible charging.

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2.6 Heat and ground pumped hydro energy storage

0

Using compressed water system to store heat. A startup and a research project have been found on this topic. No direct suppliers - GLIDES: A novel Ground Level Integrated Diverse Energy Storage (GLIDES) system which can store energy via input of electricity or heat and deliver dispatchable electricity. The proposed system is lowcost and hybridizes compressed air and pumpedstorage approaches that will allow for the offpeak storage of intermittent renewable energy for use during peak times. GLIDES, stores electricity mechanically in the form of compressed gas that displaces water in high-pressure vessels. - Insentropic: PHES Thermal Stores are split into layers to achieve high efficiency of thermal transfer, low pressure drop and higher energy density than other 'packed bed' stores. The PHES Thermal Stores work by direct heat exchange between high pressure gas and particles of crushed rock or gravel. It will be a stand-alone energy storage system called Pumped Heat Energy Storage (PHES). The cycle uses a proprietary reciprocating heat pump/engine (developed in-house). It will take electricity from the grid to charge the system.

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2.7 Ammonium - water storage tanks

0

The electricity is first transformed into the chemical potential of the working fluid by means of varying the refrigerant or absorbent mass fraction in the working fluid storage tank. When cooling, heating or dehumidifying is needed, the potential stored in the tank can then be transformed into cold/heat energy by means of absorption refrigeration/heat pump or into dehumidification/desiccation energy by means of absorption dehumidification.

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3. Mix of solid - liquid sensible heat (SL-SHS)

Back

Mix of liquid and solid heat storage


3.1 Borehole thermal energy storage (Soil storage)

0

Borehole thermal energy storage (BTES) system is an underground structure for storing large quantities of solar heat collected in summer for use later in winter. It is basically a large, underground heat exchanger. To Store solar energy in the soil under and near the building. In unsaturated soil or in rock the most interesting techniques are heat exchangers in vertical boreholes. Via these heat exchangers the energy is transferred to the ground which serves as heat capacity and is heated up to the required temperatures. Depending on the temperature level, the thermal energy is, extracted either by a heat pump (low temperature ground storage, 0°C-40°C) or directly (high temperature ground storage, 40°C-80°C) and delivered to the consumers. As a result of the limited thermal conductivity the heat losses are rather moderate and storage efficiencies of 70% can be reached. In contrast good thermal contact between the heat exchangers and the ground is required to allow a good heat transfer rate per unit area of the heat exchanger tube. In unconsolidated soils like clay, silt, or sand, heat capacity and thermal conductivity are strongly dependent on the water content especially at higher temperatures (> 60°C) . In this region water losses can occur because of vapour diffusion along the temperature gradient which can lead to dry-out and cracking in the area surrounding the heat exchanger tubes in the worst The capital cost of a large Borehole thermal energy storage system can be significant, as a large number of geothermal boreholes will need to be drilled, compared to just a few thermal wells for an ATES system. However, the installation cost should be similar to conventional GSHP systems, and the higher COP values will result in a lower total life-cycle cost than a conventional GSHP system. Both closed-loop geothermal systems will have a lower life-cycle cost than a conventional fossil-fuel fired HVAC system. Because BTES is a closed-loop geothermal technology, there should be little difficulty in obtaining permits. Typically, the most common constraint is on the available land area in which to construct the GHX array.

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4. Solid-solid latent heat storage (SS-LHS)

Back

Solid-solid phase change materials(SS-PCMs) absorb andrelease heat by reversible phase transitions between a (solid) crys-talline or semi-crystalline phase, and another (solid) amorphous,semi-crystalline, or crystalline phase. Different from solid-liquid-PCMs, solid-solid-PCMs retain their bulk solid properties withincertain temperature ranges and are therefore also referred to as ‘‘solid-state” PCMs


4.1 Inorganic

0

Inorganic SS-PCMs are able to store/release thermal energy in solid phase using one or combination of energy storage mechanisms including magnetic transformations, crystallographic structure transformations, order– disorder transformations, transformations between amorphous structure and crystal structure. In general, the amount of latent heat of inorganic SS-PCMs are smaller compared to other types of solid-solid PCMs.

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4.2 Organic

0

Organic molecules capable of reorganizing their supramolecularinteractions, typically hydrogen bonds, as a function of tempera-ture, can potentially undergo highly endothermic solid-solid phasetransitions. These highly symmetric and bulky alcohols, such aspentaerythritol (PE), neopentylglycol (NPG), trimethylol propane(TMP), and pentaglycerine (PG).

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4.3 Organo-Metallic

0

Organometallic SS-PCM are a group of layer perovskite organometallics, which are composed of alternate inorganic and organic layers and have a sandwich-like crystalline structure. The pure compounds exhibit relatively high latent heats for their solid-solid phase transitions (above 100 J/g), at temperatures ranging from 40°C to 190°C. The transition temperatures can be tuned by producing eutectic mixtures of two of these compounds,in general lowering both the transition temperature and the phase-change latent heats

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4.4 Polymeric

0

Attachment or incorporation of a phase changing motif into a polymeric structure will be accompanied by a decrease in the observed latent heat. This reduction on the energy absorbed during the phase transition is due to several factors: (a) dilution of the phase changing moieties within a thermally inert polymeric matrix, (b) mobility or packing restrictions of the crystallizing groups due to attachment, (c) strong interaction of the phase changing moieties with the polymer backbone. The magnitude of the decrease in the observed latent heats depends on the choice of polymer backbone and phase changing motifs. Also more information available [here](https://reader.elsevier.com/reader/sd/pii/S1359431117329939?token=F3E55D40A856580F2188E89A722387D50B5EA5DF9D550BFDE7F622789008B95FE03FE254E5D8DF93A9010EE6953547D0).

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5. Solid-liquid latent heat storage (SL-LHS)

Back

Generally, LHS systems use the latent heat between solid andliquid phases of the storage medium, whereby the PCM is requiredto be contained or encapsulated within a container to prevent theliquid from leaking; however, the capsules decrease the energydensity of the system and increase the cost of production. Such storage has potential in heating and cooling buildings, waste heat recovery, offpeak power utilization, heat pump systems, tanks and many other applications


5.1 Non-parafins (Organic)

0

The non-paraffin organic (fatty acids, esters, and alcohols) are the most numerous of the phase change materials with highly varied properties. They are highly flammable and therefore, should not be exposed to intense temperature, flames or oxidizing agents . Non-paraffin organic materials are further subgroups as fatty acids and other non-paraffin organic materials. Among the non-paraffin organic PCMs, fatty acids are relatively cheaper, although their cost remains 2–2.5 times higher than technical grade paraffin's https://www.global-e-systems.com/en/products/gaia-pcm-thermal-energy-storage-ball/

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5.2 Parafin (Organic)

0

Paraffin are non-corrosive, chemically inert and stable below 500 °C, show little volume changes on melting and have low vapor pressure in the melt form, therefore are one of the more utilized PCM, Paraffin is a petroleum derivative organic material (an alkane hydrocarbon with long straight n-alkane chains as the composition of “CH3− (CH2)n – CH3”) chemically inert and stable below 500 °C. They have many other characteristics such as repeated melting and freezing without phase segregation and consequent degradation of their latent heat of fusion, low vapor pressure during melting, crystallize with little or no super cooling condition, noncorrosive, chemically stable, low cost and largely available. However, they present low thermal conductivity, are non-compatible with the plastic container and flammable. These adverse properties can be improve and solved by encapsulating the paraffin in a suitable container

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5.3 Metallic alloys (Inorganic)

0

Constraints, due to high volumetric fusion heat, they are a good candidate. The use of metal/metallic materials poses a number of engineering problems during design, development and exploitation of the storage system. T A new concept of MgH2 tank was developed to store the heat of reaction by using a phase-change material (PCM). The heat of desorption is mainly provided by the latent heat of solidification of the PCM. Ex: A metallic alloy based on Mg–Zn eutectic was selected as PCM in order to enhance the thermal exchange with the MgH2 compacts

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5.4 Salt Hydrates and compositions (Inorganic)

0

The solid–liquid transformation of salt hydrates is actually dehydration of salt that resembles melting or freezing thermodynamically [84]. Salt hydrates can be considered as alloys of inorganic salts (AB) and water (H2O), resulting in a typical crystalline solid with a general formula (AB x H2O) [84,95]. A salt hydrates usually melts to either to a salt hydrate with fewer moles of water or to its anhydrous form. During the charging phase, the thermal energy is stored by performing the dehydration reaction of a hydrated salt. During the discharging phase, the stored heat is released by undergoing the hydration reaction of the salt. This process is achieved by addition of water vapor to anhydrous salt In general, inorganic compounds have near twice the energy storage capacity per volume unit than organic compounds and they possess much higher operating temperatures. Salts have been extensively studied for their use in LHTES systems. They present a high latent heat of fusion per unit volume, a higher thermal conductivity than paraffin׳s and small volume changes on melting also compatible with plastics, non-flammables, but are slightly toxic, present supercooling and nucleation problems and corrosive to most metals. The high heat of fusion of chlorides and fluorides, and the low cost of the former have encouraged further studies of salt compositions on their basis.

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5.5 Eutetic phase change materials

0

Organic and Eutetic phase change material operate on the same principle as inorganic (as salt) PCM. Research on these components has mostly been initiated by some obvious disadvantages of salt PCM, such as being corrosive, being incompatible with several materials, experiencing supercooling and segregation during phase transition under thermal cycling. A large number of organic PCMs are available in the temperature range from −5 °C to 190 °C. Depending on the type of applications, the organic PCMs should first be selected based on their phase change temperature. Materials that exhibit phase change below 15 °C are used in cooling applications, while materials that have phase change above 90 °C are used for absorption refrigeration. The organic PCMs and their mixtures that show phase change around 18–65 °C are suitable for the thermal comfort applications in textiles and in buildings.

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5.6 Alkanes

0

A method for characterization of alkanes (C1,-C100) and paraffin waxes for application as the low-temperature (298-323 K) phase change energy storage medium is introduced.It is demonstrated that the family of n-alkanes has a large spectrum of latent heats, melting points, densities, and specific heats so that the heat storage designer has a good choice of n-alkanes as storage materials for any particular low-temperature thermal energy storage application.

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5.7 Fine powdered composite for latent heat storage [R]

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Sorption heat storage implies the use of physical or chemical bonds to store energy. The principle of sorption occurs during a reaction, and in order to take place, at least two components are needed: a sorbent, which is typically a liquid or solid, and a sorbate, which is typically a vapor. During the charging process, an endothermic reaction occurs, and the sorbent and sorbate are separated. The two components can then be stored separately, ideally without energy losses. During the discharging process, sorbent and sorbate react producing an exothermic reaction that releases heat. The main advantages of sorption heat storage are higher energy density and negligible heat losses compared to a conventional thermal storage based on sensible heat. A conventional water storage needs to be approximately five to ten times larger than a sorption heat storage system for storing the same energy. In this specific case, the system uses the reaction energy created when salts are hydrated or dehydrated. It can work by storing heat in a container containing 50% sodium hydroxide (NaOH) solution. Heat (e.g. from using a solar collector) is stored by evaporating the water in an endothermic reaction. When water is added again, heat is released in an exothermic reaction at 50 °C (120 °F). Generally, current systems operate at 60% efficiency. The system is especially advantageous for seasonal thermal energy storage, because the dried salt can be stored at room temperature for prolonged times, without energy loss. The containers with the dehydrated salt can even be transported to a different location. The system has a higher energy density than heat stored in water and the capacity of the system can be designed to store energy from a few months to years.

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5.8 Ice/Water Heat pipe for cold storage

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Seasonal cold storage is a high efficient and environmental friendly technique that uses the stored natural cold energy in winter (e.g., snow, ice or cold ambient air) for free cooling in summer. This paper presents a seasonal cold storage system that uses separate type heat pipes to charge the cold energy from ambient air in winter automatically, without consuming any energy. The charged cold energy is stored in the form of ice in an insulated tank and is extracted as chilled water for cooling supply in summer, which help to reduce the chiller running time and reduce the associated electricity consumption and greenhouse gas emission significantly

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5.9 Heat Pipes

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Heat pipes are used in many applications – as one of the most efficient heat exchanger devices – to amplify the charging/discharging processes rate and are used to transfer heat from a source to the storage or from the storage to a sink

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6. Latent Integration technologies

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Technolgies to integrate Phase Change Materials into processes.


6.1 Building materials filled with PCM

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PCM used in building materials. **_Example:_** - The incorporation of PCMs into building envelope solutions takes advantage of solar energy, contributing to the overall reduction of energy consumption associated to use of the air conditioning systems - Use of phase change materials (PCM) in concrete pavements to store heat, which can be used to reduce ice formation and snow accumulation on the surface of the concrete pavement.

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6.2 Phase Change Material in water tanks

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In recent years, latent heat storage systems have been increasingly used in building energy conservation, solar heating systems, and waste heat recovery systems. The water tank as a key component of solar heating systems has been widely applied in practical applications.

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6.3 Bed Storage concept

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High heat transfer coefficients can be achieved between a fluidized bed of coated PCM particles and a heat exchanging surface[7]: heatcan be captured by the particulate gas–solid flowing suspension. **_Example of installations:_** - Packed beds - Fluidized beds - Encapsulated in fluidized beds

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6.4 Heat exchanger integration

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Integration of PCM into heat exchangers. **_Examples of application:_** - The tanks are connected through a salts-heat transfer fluid heat exchanger, which is coupled to the heat source and the heat sink. - The latent heat TES technology is evaluated in a 0.154 m3 storage tank based on the shell-and-tube heat exchanger concept which is connected to a heat source and a heat sink simulating the waste heat recovery of an industrial process [36]. The material used is 99.5 kg of high density polyethylene (HDPE). - directcontact heat exchanger using erythritol (melting point: 391 K) as a phase change material (PCM) and a heat transfer oil (HTO) for accelerating heat storag

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6.5 High temperature concrete as storage media

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A three component thermal storage system, combining sensible and latent heat storage where the PCM are encapsulated in concrete.

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6.6 Micro encapsulated PCM

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Micro-encapsulated PCM slurry is a suspension where the PCM is dispersed at 10–20 wt % without significantly altering the physical properties of the liquid (density, viscosity) **_Exampl:e_** - PCM is microencapsulated using a polymeric capsule and dispersed in water. - also used in Slurries and Molten Salt

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6.7 Nano PCM

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The main drawback of encapsulated PCMs is their low thermal conductivity, hence the growing interest in dispersing high conductive nanoparticles within the PCMs. **_Example:_** - Different metal nanoparticles in order to enhance the thermal conductivity of paraffin wax. T

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6.8 Supercooling

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Supercooling, subcooling or undercooling is when a phase change material in liquid state cools down below its melting point without solidifying; leaving it in a metastable state where the latent heat of fusion is not released. In latent heat storage supercooling has traditionally been seen as an undesired effect that had to be avoided as it prevented the heat of fusion from being released when the melting point of the storage material was reached during the discharge process The idea of utilizing supercooled salt hydrates for long term storage has however been known since the late 1920s and pocket-sized heat packs storing heat in supercooled sodium acetate trihydrate were patented in 1978. This principle makes long term thermal energy storage possible by letting the melted salt hydrate remain in supercooled state at ambient temperature in the storage period. Once the heat is needed the solidification of the supercooled solution is triggered and the latent heat of fusion is released as it crystalizes. Investigations have previously shown that there is a potential in utilizing stable supercooling as a storage technique

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6.9 Adsorption pump

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A study dedicated to an inter-seasonal heat storage process based on novel absorption pump operated in two half-cycles that uses LiBr/H2O as the absorbent/absorbate couple. The solar energy is stored during summer through desorption, and the heat is released during winter through absorption. A characteristic of the device is that crystallization occurs in the storage tank as its temperature falls under 10 °C at the end of summer or in winter.

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6.10 Steam integration

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The low thermal conductivity of PCM is enhanced by using extended aluminum fins that are attached to the baking plate and extruded inward to the storage. In this paper, twophase loop thermosyphon of steam is used to manage the long distance heat transportation required between the receiver (outside) and the storage (inside a house). The steam in the thermosyphon flow has restricted to a maximum working temperature of 250oC. Steam is selected for its highest heat capacity, availability and stable nature. It carries heat from the collector focus point and condenses in a coiled pipe imbedded in aluminum plate placed on top of the storage

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6.11 Heat pipes filled with PCM

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Integrating PCM with heat pipes. **_Examples:_** - The issue of the low conductivity of PCMs has been addressed by using an embedded finned watercharged heat pipes into the PCM bulk The approach is to physically decouple the evaporator pipes from the PCM, thus allowing independent sizing of each component. - The thermal link between the two components is done via evaporation and condensation of a heat transfer fluid (HTF), according to the principle of a heat pipe. Pumping the liquid HTF provides active control of the heat pipe operation. The new concept is modeled and compared to the conventional design of conduction based PCM annulus around the steam pipe

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6.12 Supercritical fluids with PCM

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The use of supercritical fluids allows cost affordable high density storage with a combination of latent heat and sensible heat in the two phase as well as the supercritical state. This technology will enhance penetration of several thermal power generation applications and high temperature water for commercial use if the overall cost of the technology can be demonstrated to be lower than the current state of the art molten salt using sodium nitrate and potassium nitrate eutectic mixtures.

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6.13 Metal foams

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Metal foams have also been proven to be a viable option in enhancing thermal conductivity of PCMs. High porosity, good thermophysical properties and mechanical strength are salient features of metal foams.

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7. Thermochemical heat storage (THS)

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THS systems can utilise both sorption and chemical reactions to generate heat and in order to achieve efficient and economically acceptable systems, the appropriate reversible reactions (suitable to the user demand needs) need to be identified


7.1 Hydroxides (M(OH)2)

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The dehydration reaction of metal hydroxides can lead to high heat storage efficiency and places these chemicals as candidates for thermochemical heat storage. Based on Ca, Mg, Be, Mn, Sr, Ba, Ni, Zn, Cd

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7.2 Metal Carbonates (MCO3)

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Metal carbonates have mainly been proposed and studied as sorbent materials in the context of CO2 capture. The capture and storage of carbon dioxide has become of prime interest in order to reduce the concentration of greenhouse gases in the atmosphere and as such, literature data on the thermal behavior of sorbents (especially calcium oxide-based sorbents) during carbonation/calcination looping cycles is abundant. Metal carbonates are also potential candidates for thermochemical heat storage with some of them showing remarkable high reaction enthalpy and energy storage density Based on Ca, Sr, Mg, Ba, Cd, Zn, Pb

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7.3 Metal sulfates (MSO4)

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Metal sulfates have been studied for application as heat storage media for solar energy. Metal sulfates are potential candidates for thermochemical heat storage because they exhibit high reaction enthalpies and can be suitable for operating with concentrated solar energy since their operating temperatures are comprised between roughly 900 °C and 1400 °C . Based on Mn, Fe, Co, Cu, Ba, Zn, Cd, Ni

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7.4 Pure metal oxides (MO)

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Various metal oxides have been studied for thermochemical heat storage applications due to their high gravimetric storage density, which is important for lowering the necessary amount of reactant involved in large-scale process. Based on Rh, V, Ca, Mn, Cu, Li, Fe, Ba, Ng, Cr, Pt, Pb, Sb, U, Mg

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7.5 Zeolite

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Zeolites are crystalline alumino-silicates, characterized by a high specific surface area (i.e., about 800 m2/g) and wide microporous volumes, which make these materials perfectly suitable for water vapor adsorption. Owing to their porous structure, zeolites are usually highly hydrophilic, which allows them to obtain high adsorption capacities even at low partial pressures. This high affinity with water, of course, is reflective of strong bonding that requires higher temperatures to be broken compared to silica gels (i.e., more than 150 °C). Zeolites type A, 13X and Y are the most common classical synthetic zeolites employed for adsorption heat storage. These materials are mostly used for open adsorption TES, since, in order to get enough energy storage density, they must be regenerated at high temperatures, making air the most effective heat transfer medium. Thus, due to the required high operation temperature, they are usually employed for industrial waste heat recovery and storage

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7.6 Silica Gel

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Silica gels historically represent one of the most employed adsorbent materials for water vapor adsorption. In fact, they represent a less expensive option for adsorption TES applications and can be easily employed for heat sources at temperatures lower than 100 °C (e.g., flat-plate solar thermal collectors). It is important to highlight that the porous structure of silica gels for closed adsorption TES must be completely different from that which is employed for open adsorption TES. Indeed, as in a closed system the adsorption/desorption process usually occurs in a limited partial pressure range (e.g., between 0.1 and 0.3 p/p0), it is necessary to have silica gels with highly microporous structures, capable of exchanging high quantities of water vapor. On the contrary, in an open adsorption TES, since the working partial pressures are usually higher, a mesoporous silica gel can be also employed, due to the capillary condensation phenomena that occurs within this working range.


7.7 Zeo-like Materials

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their crystalline structure is somewhat similar to those of classical zeolites. The two classes that showed the most promising features are the aluminophosphates (AlPOs) and the silico-aluminophosphates (SAPOs). Indeed, in contrast to other classical adsorbents, these materials show a partially hydrophobic behavior, that is reflected in an S-shaped adsorption isotherm. This is an advantageous characteristic, that allows a high amount of water vapor exchange to be obtained in a narrow range of partial pressure. Accordingly, since the overall heat storage capacity is highly dependent on the water vapor exchange, these materials can guarantee very high heat storage capacities. Among these two classes, the most attractive materials are known as AlPO-18 and SAPO-34


7.8 Composite

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Composite sorbents represent a hybrid method to enhance the sorption ability of materials under the typical working boundary conditions of adsorption TES [13]. Indeed, they are based on the embedding of inorganic salt (e.g., CaCl2, LiCl, LiBr) inside a host porous structure (e.g., silica gel, vermiculite, zeolites).


7.9 Metal Hydrides

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A metal hydride energy store for CSP operates through the highly endothermic and exothermic processes of hydrogen desorption and absorption, respectively. The metal hydride in question (designated as the HT (high temperature) hydride) will be heated during a day-cycle from solar energy and will release hydrogen. This hydrogen gas must then be stored. The hydrogen can either be stored in a volumetric gas tank or another metal hydride that operates at LT (low temperature).

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Final Results

Published 09/24/2019

After the midway results meeting, 45 technologies to store heat have been reviewed and deepened. The results are organised based on the concept and presented per technologies to store heat comprising a description, findings, suppliers (if applicable), images, videos, useful links and a reference list. The technology requirements are measured and shown in the [requirements table](#requirements-table). By using the concept links below, you can quickly navigate to the concepts and their technologies to store heat descriptions.

Table of concepts:

  1. 1. Solid sensible heat storage (S-SHS)
  2. 2. Liquid sensible heat storage (L-SHS)
  3. 3. Mix of solid - liquid sensible heat (SL-SHS)
  4. 4. Solid-solid latent heat storage (SS-LHS)
  5. 5. Solid-liquid latent heat storage (SL-LHS)
  6. 6. Latent Integration technologies
  7. 7. Thermochemical heat storage (THS)

Technology Radar
Requirements Table

1. Solid sensible heat storage (S-SHS)

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Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on solid materials. General advantages of sensible heat storage: * Simple applications with widely available materials * Long lifetime of systems (many cycles possible) * Cost-effectively * Able to store energy for a long period of time * Unhazardous and low-cost materials * Easy to control and reliable systems General disadvantages of sensible heat storage: * A Large volume required to store the energy (low energy density) * Possible geological requirements * Heat loss to the ambient environment (reduces efficiency over time)


1.1 Concrete storage pile

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The use of concrete geostructures for energy extraction and storage in the ground is an environmentally friendly and easy way of cooling and heating buildings. With such energy geostructures, it is possible to transfer energy from the ground to buildings by means of fluid-filled pipes cast in concrete. By injecting thermal energy in summer and extracting it in winter, the ground in the area of a building’s piles can be used for seasonal energy storage, as long as the underground water flow in the storage remains low. Most buildings use piles for the foundation, and these piles can easily contain heat exchangers in contact with the soil. The so-called ‘energy pile’ can thus fulfill a double function: foundation plus heat exchange. Heat pumps can then transfer heat very efficiently from the ground to be building interior and vice-versa. Heat exchange with the ground can be via thermo-active foundations. In thermo-active foundations, foundation piles also referred to as "thermal piles" or as "energy piles", are used as heat exchangers for supplying low-temperature heat to heat pumps. They can also be used for underground storage of warmth supplied by road solar collectors. Some suppliers also propose heat storage in concrete piles as a flexible installation that is not used as a building foundation and can be used as an add on to an existing building or district (see Energy Nest). Concrete has a density around 2240 kg/m³ with a specific heat capacity of 880 J/kg K. This results in an average storage density of 1971 kJ/m³ K. The thermal conductivity of reinforced concrete is around 1.5 W/m K. ***Applications:*** * Building / Residential storage * Separate storage units containers (Energy Nest)

1.1.1 Concrete storage pile
CONCRETE STORAGE FOR SOLAR THERMAL POWER PLANTS AND INDUSTRIAL PROCESS HEAT
Economic storage of thermal energy is a technological key issue for solar thermal power plants and industrial waste heat recovery. Systems using single phase heat transfer fluids like thermal oil, pressurized water, air or superheated steam, demand storage systems for sensible heat. A sensible heat storage system using concrete as storage material has been developed by Ed. Zublin AG and DLR. A major focus was the cost reduction of the heat exchanger and the high temperature concrete storage material. For live tests and further improvements a second generation 20 m³ solid media storage test module was built in Stuttgart and is cycled by an electrically heated thermal oil loop. By end of October 2008 the second generation solid media storage test module had accumulated four months of operation in the temperature range between 300 °C and 400 °C and about 50 thermal cycles with a temperature difference of 40 K. The tests will be continued until June 2009. Application fields for the concrete storage technology are parabolic trough solar thermal power plants; industrial waste heat recovery at elevated temperatures; thermal management of decentralized combined heat and power systems for increased flexibility and other high temperature processes. Especially the wide range of possible working temperatures and the modular structure make the heat storage in concrete attractive.
11/01/2008 00:00:00
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1.1.2 Concrete storage pile
Development of Solar Energy Underground Seasonal Storage Device and Its Parameters Measuring System
In order to improve the availability of solar energy, this paper introduces a new solar energy storage device and its parameters automatic measuring system. The device puts the heat which was gathered by synchronous tracking solar collector into underground concrete storage pile. Meanwhile, the system could simultaneously measure the temperature, pressure and flow of the device, etc. Some derived parameters such as thermal energy storage and thermal storage effectiveness can be obtained by calculation. According to the experimental results, the device is able to store the solar energy for seasons in the underground, and automatic measuring system could display the parameters and real-time curves on monitor and draw the history curves of all parameters. The data base of parameters could be built during the energy storage process. Furthermore, the energy storage report can be generated to obtain an automatic and digital energy storage process.
08/01/2010 00:00:00
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1.1.3 Concrete storage pile
Experimental investigation of sensible thermal energy storage in small sized, different shaped concrete material packed bed
Purpose Solar energy varies with time, intermittent; an accumulator unit is required to attach with collectors to collect energy for use when the sunshine is not available. This paper aims to design a system for storing the solar sensible heat thermal energy. Design/methodology/approach This paper presents the design and experimental evaluation of sensible heat thermal energy storage (TES) system for its energy storage performance by varying the air flow rate and packing material shape. Heat transfer fluid as air and solid concrete material of high density of different shapes were used for storage. Findings This paper presents the evaluation of data of number of experimental observations on the system. It was found that charging/discharging was based on the shape of the material and void fraction. Originality/value This paper provides the data for designing the TES, considering the concrete as storage material and shape of material for optimizing the system.
10/03/2016 00:00:00
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1.1.4 Concrete storage pile
Geothermal cooling and heating using enercret thermo-active foundations project study, new office building ademe-angers, France
Concrete structures such as piles, diaphragm walls, retaining walls, foundation slabs etc. are used to absorb thermal energy from the ground and ground water (ground temperature is approx. 13 °C in central Europe). The energy is absorbed and transported by means of fluid-filled pipe systems incorporated inside the foundation elements which are needed for structural reasons. A building can be cooled for next to nothing by using the cooling fluid. In the case of heating the same system can be used to extract energy by means of a heat pump. The ground provides an intermediate storage facility for excess energy - the warmth disposed during cooling period can be absorbed for heating and vice versa. For the new office building of ADEME-Angers, investigated in this study, Enercret provides energy savings of 71%, CO 2 emissions of almost zero, and a payback time of 4.71 years.
01/01/2001 00:00:00
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1.1.5 Concrete storage pile
High-Temperature Solid-Media Thermal Energy Storage for Solar Thermal Power Plants
Solid sensible heat storage is an attractive option for high-temperature storage applications regarding investment and maintenance costs. Using concrete as solid storage material is most suitable, as it is easy to handle, the major aggregates are available all over the world, and there are no environmentally critical components. Long-term stability of concrete has been proven in oven experiments and through strength measurements up to 500 ° C. Material parameters and storage performance have been validated in a 20-m 3 test module with more than 23 months of operation between 200 ° C and 400 ° C and more than 370 thermal cycles. For an up-scaled concrete storage design with 1100-MWh capacity in a modular setup for a 50 MW el parabolic trough power plant of the ANDASOL-type, about 50 000 m 3 of concrete is required and the investment costs are approximately 38 million euro. The simulation of the annual electricity generation of a 50 MW el parabolic trough power plant with a 1100-MWh concrete storage illustrates that such plants can operate in southern Europe delivering about 3500 full load hours annually; about 30% of this electricity would be generated by the storage system. This number will increase further, when improved operation strategies are applied. Approaches for further cost reduction using heat transfer structures with high thermal conductivity inside the concrete are analyzed, leading to a 60% reduction in the number of heat exchanger pipes required. For implementation of the structures, the storage is build up of precast concrete blocks.
02/01/2012 00:00:00
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1.1.6 Concrete storage pile
Hydrothermal Modeling of Pile Heat Exchangers in the Unsaturated Zone
Pile heat exchangers (PHE) are an attractive way to exchange thermal energy with shallow underground since they combine the structural role of geostructures with ground heat exchangers, making it possible to mutualize both investments. PHE are typically 5 to 20 m deep and can be partially located in the unsaturated (vadose) zone. Thermal properties of soil depend on water content, which is heterogeneous in the unsaturated zone. The presented study investigates the influence of groundwater table depth upon the amount of heat transferred by the PHE. It is a part of a research project ‘‘GECKO’’ (geo-structures and hybrid solar panel coupling for optimized energy storage) which is supported by a grant from the French National Research Agency (ANR). The authors focused on deriving an effective thermal conductivity of the ground, denoted ¯(λ_m ), as this value is essential to a consistent PHE sizing. A three-dimensional finite elements (FE) model developed in COMSOL-Multiphysics ® of a 10 m deep PHE has been set up. The geometry of the pipes, pile concrete and surrounding ground is discretized. Stationary distribution of matric potential is determined by solving the Richards equation while the resolution of the heat equation leads to the temperature evolution in the heat-carrier fluid, the concrete and the surrounding ground. Several cases were modelled for ground water table depths ranging from 0.5 m to 9.5 m (cf. Figure 1). The two mentioned bounds respectively correspond to situation where the PHE stands in almost saturated or unsaturated soil. The considered soil, a homogenous Fontainebleau sand, is subject to large water content variations which lead to large thermal conductivity variations: The estimated thermal conductivity is 3.01 W.K-1.m-1 at saturation, i.e. matric potential ψ = 0 m, and 0.46 W.K-1.m-1 for ψ = -10 m. Other soils ranging from clay to sandy loam exhibit a smaller influence of moisture content and matric potential upon thermal conductivity. To determine an effective thermal conductivity of the ground ¯(λ_m ) the PHE was subject to a thermal response test (TRT) – i.e. a constant power given to the heat-carrier fluid. ¯(λ_m ) was estimated based on the evolution of fluid temperature, according to state-of-the-art procedures for TRT interpretations. The analytical model used for the interpretation considers that the pile behaves as an infinite line emitting a constant heat flow in a homogenous media. ¯(λ_m ) is tuned so that the evolutions of inlet/outlet averaged fluid temperatures computed by both models (FE and analytical) match. As a result, ¯(λ_m ) ranges from 3.01 ± 0.01 W.K-1.m-1 for a groundwater level depth of 0.5 m to 1.33 ± 0.04 W.K-1.m-1 for a groundwater level depth of 9.5 m. The effective thermal conductivity ¯(λ_m ) is almost identical to the ground conductivity averaged over the PHE height. These preliminary results suggest that for a single PHE standing in an unsaturated soil the temperature evolution of the heat-carrier fluid can correctly be described by an analytical model considering a homogenous media whose thermal conductivity is equal to the averaged ground conductivity. Further development should focus on similar study for a group of PHE.
04/08/2015 00:00:00
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1.1.7 Concrete storage pile
Numerical analysis of seasonal heat storage in an energy pile foundation
The use of concrete geostructures for energy extraction and storage in the ground is an environmentally friendly and easy way of cooling and heating buildings. With such energy geostructures, it is possible to transfer energy from the ground to buildings by means of fluid-filled pipes cast in concrete. By injecting thermal energy in summer and extracting it in winter, the ground in the area of a building’s piles can be used for seasonal energy storage, as long as the underground water flow in the storage remains low. This paper is a contribution to the improvement of the knowledge in the field of energy geostructures. The behaviour of a multi-pile seasonal storage system subjected to thermo-mechanical loading is examined numerically from both thermal and mechanical perspectives. The purpose of this paper is (i) to propose a thermo-hydro-mechanical 2D solution to the 3D problem, (ii) to explore the thermal behaviour of this type of storage and (iii) to evaluate its structural consequences. Coupled multi-physical finite element modelling is conducted. The efficiency of the storage is not dramatically affected by an increase in the annual mean temperature of the storage. It is shown that induced mechanical loads are less important when considering a wholly heated pile structure than when considering a single heated pile in a foundation. The evolution of stresses in the piles and in the soil during heating–cooling cycles also reveals possible critical phenomena.
01/01/2014 00:00:00
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1.1.8 Concrete storage pile
Research on Solar Energy Underground Seasonal Storage Device and Its Parameters Measuring System
In order to improve the availability of solar energy, this paper introduces a new solar energy storage device and its parameters automatic measuring system. The device puts the heat which was gathered by synchronous tracking solar collector into underground concrete storage pile. Meanwhile, the system could simultaneously measure the temperature, pressure and flow of the device, etc. Some derived parameters such as thermal energy storage and thermal storage effectiveness can be obtained by calculation. According to the experimental results, the device is able to store the solar energy for seasons in the underground, and automatic measuring system could display the parameters and real-time curves on monitor and draw the history curves of all parameters. The data base of parameters could be built during the energy storage process. Furthermore, the energy storage report can be generated to obtain an automatic and digital energy storage process.
05/03/2011 00:00:00
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1.1.9 Concrete storage pile
Thermal performance of a concrete column as a sensible thermal energy storage medium and a heater
Abstract A square sectioned concrete column was constructed with its real dimensions in order to investigate the thermal performance of the concrete column which is proposed to be used as a heater and thermal energy storage medium in the building structure. For this purpose, a steel pipe was inserted in the lengthwise of the concrete column for air flow to store thermal energy from heated air to concrete column. Thermal performance of the column was investigated experimentally for various air flow temperatures and velocities as a function of operation time. Results of a week showed that concrete column can be used as a heater and also thermal energy storage medium in the building structure. In addition, it was shown that amount of heat released from concrete column can be controlled by air flow temperature, flow velocity and energy charging time. Investigated concrete column was also modeled three-dimensional by a CFD code and transient numerical results were validated by experimental results. The obtained high agreement with realizable k-epsilon turbulence model showed that CFD codes could be used for pre-calculations of the experiments and for numerical modeling of multi-story building with this novel heating system that is hard and expensive to study experimentally.
10/01/2017 00:00:00
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1.2 Granular materials (Sand and rocks)

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Granular materials such as sand and rocks are studied to present an additional HTF to represent an efficient and cost-effective alternative. Low-cost solid particulates can store and transport heat at temperatures over 1000 °C. Sand has an average density of 1555 kg/m³ and rock around 2560 kg/m³ with their specific heat 800 (J/kg K) and 879 (J/kg K). This results in a range of storage capacity depending on the amount of rock/sand. The range is from 1244 to 2250 kJ/m³ K. ***Examples:*** * Dead Sea salt, concrete bed, and Basalt rocks are more economically attractive relative to molten salt plant because they eliminate the extra cost associated with freeze protection, no pressurizing problem, no corrosion. Finally, natural stones can operate at a higher temperature and do not suffer from cracking due to cyclic charging and discharging. * For the purpose of heat recovery, a moving bed heat exchanger (MBHX) is applied and tested. In this study, the dense granular mass is gravity-driven through a heat exchanger. The performance of the MBHX with the utilization of Sand, Basalt, and a Mixture of Sand and Basalt as a granular material was experimentally investigated. It is found that the effectiveness of the MBHX using a mixture of 50% sand and 50% basalt improved by 30% compared to using sand alone. * Also used based on rock storage as in the 30 MWh Hamburg-Altenwerder power plant. Its pilot ETES facility, which stores energy in 1,000 tonnes of rockfill at temperatures of 600 °C, is currently in its final phase of construction and is due to be fully commissioned in 2019. Heat energy stored in the rock fill can be converted back into 30 MWh of electricity by a steam turbine. The facility addresses the issue of how to balance supply and demand when integrating intermittent renewable energy sources – such as wind – into the energy system, the manufacturer explained. Storage facilities can be used to buffer periods of low wind or solar production, Siemens Gamesa added – when the air is still or the sun is not shining. ***Applications:*** * Large scale industrial storage * Concentrated solar power plants

1.2.1 Granular materials (Sand and rocks)
Innovative sensible heat transfer medium for a moving bed heat exchanger in solar central receiver power plants
Renewable energies are gaining importance due to the steadily increasing scarcity of fossil fuels, the ongoing climate change and last but not least the risks which accompany the use of nuclear power. In this growing market, solar thermal power plants offer a centralized, potentially load following electricity production. To serve this need, the integration of thermal energy storage systems is essential. The Moving Bed Heat Exchanger MBHX storage concept for CSP systems using sensible heat transfer medium aims at using a low cost solid storage media. This concept requires intermediate bulk cycles to transfer heat between the solar field and the storage material (the bulk). Heat Transfer Fluids (HTF) such as synthetic oils (mobiltherm 603) are typically used. In this work, granular materials such as sand and rocks are studied to present an additional HTF to represent an efficient and cost-effective alternative. Low cost solid particulates can store and transport heat at temperatures over 1000°C. For the purpose of heat recovery, a moving bed heat exchanger (MBHX) is applied and tested. In this study, the dense granular mass is gravity-driven through a heat exchanger. The performance of the MBHX with the utilization of Sand, Basalt, and a Mixture of Sand and Basalt as a granular material was experimentally investigated. It is found that the effectiveness of the MBHX using a mixture of 50% sand and 50% basalt improved by 30% compared to using sand alone.
04/01/2017 00:00:00
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1.2.2 Granular materials (Sand and rocks)
Optimal design for sensible thermal energy storage tank using natural solid materials for a parabolic trough power plant
Abstract This paper presents numerical investigation of transient behavior and thermal storage capability of a sensible heat storage (SHS) unit designed for storing heat in the temperature range of 523–673 K. The objective of this study is to assess the potential of using two candidate materials as energy storage media found in Jordan. The thermal performance of using these materials in SHS tank is compared against concrete bed. A heat storage unit of cylindrical configuration with embedded charging tubes has been designed. To investigate their heat storage characteristics, a finite element based 3-D mathematical model has been developed using COMSOL Multiphysics 5.1. Numerically predicted results match closely with the data reported in the literature. Performances of the thermal storage bed of capacity of 136.7 MW in 3 h (including charging time, energy storage rate, charging energy efficiency) have been evaluated for the selected three storage materials. In order to optimize the design of energy storage tank, parametric studies are carried out by varying the number of the charging tubes, diameter of charging tubes, fins effectiveness, and storage bed diameter to its height. Simulations results showed that overall thermal performance of these materials using optimal design are satisfactory considering the problems associated with molten salt and concrete bed. More specifically, Dead Sea salt, concrete bed and Basalt rocks are more economically attractive relative to molten salt plant because they eliminate the extra cost associated with freeze protection, no pressurizing problem, no corrosion. Finally, natural stones can operate at higher temperature and do not suffer from cracking due to cyclic charging and discharging.
09/01/2018 00:00:00
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1.3 Natural Rock/cavern storage

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TES system using underground rock carven is considered as an attractive alternative for largescale storage, because of low thermal conductivity and chemical safety of surrounding rock mass. Based on some successful applications of cavern storage and high-temperature storage reported in the literature. The applicabilities and practicabilities of storage media and technologies for largescale cavern thermal energy storage (CTES) were reviewed. Ex: Basalt rocks Natural cave storge can be based mostly on rock and granite. Rock was mentioned in 1.2 with a storage capacity of 2250 kJ/m³ K. Granite has a density of 2640 kg/m³ with a specific heat capacity of 820 J/kg K, giving a storage capacity of 2164 kJ/m³ K. ***Applications:*** * Large scale

1.3.1 Natural Rock/cavern storage
Review on Thermal Storage Media for Cavern Thermal Energy Storage
Developing efficient and reliable energy storage system is as important as exploring new energy resources. Energy storage system can balance the periodic and quantitative mismatch between energy supply and energy demand and increase the energy efficiency. Industrial waster heat and renewable energy such as solar energy can be stored by the thermal energy storage (TES) system at high and low temperatures. TES system using underground rock carven is considered as an attractive alternative for large-scale storage, because of low thermal conductivity and chemical safety of surrounding rock mass. In this report, the development of available thermal energy storage methods and the characteristics of storage media were introduced. Based on some successful applications of cavern storage and high-temperature storage reported in the literature, the applicabilities and practicabilities of storage media and technologies for large-scale cavern thermal energy storage (CTES) were reviewed.
08/31/2012 00:00:00
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1.3.2 Natural Rock/cavern storage
Solar energy storing rock-bed to heat an agricultural greenhouse
Abstract The quality requirements of crops, particularly for export, are causing more and more Moroccan producers to consider heating their greenhouses. As the heating costs by conventional energy sources (coal, oil and natural gas) is too high, especially for developing countries, the use of renewable energy technologies and systems to heat the greenhouses have gained much attention in recent years. In this context, to maintain the optimum growth environment for plants, a solar energy storing rock-bed has been used to heat the ambient air inside a canarian type greenhouse. This system stores excess heat from the greenhouse during the day and restitutes it at night. The results of experimental measurements of the climatic parameters show that air temperature inside the greenhouse equipped with rock-bed is on average 3 °C higher than inside the conventional greenhouse during the night and 1.9 °C lower during the day. As the greenhouse equipped with the solar energy storing system was cooled down during the day and heated-up at night, its relative humidity was naturally higher during the day and lower at night. In addition, this system has a positive effect on the tomato yield, which has been improved by 22% compared to the conventional greenhouse.
02/01/2019 00:00:00
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1.4 Sand

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Seasonal sandbed solar thermal storage systems are an excellent option for storing heat for climates in regions with long periods of freezing temperatures. The present study shows a proof of concept of a sandbed seasonal solar thermal storage that needs additional controls for residential heating application. The system could also be used to provide heat for unoccupied spaces such as garages and greenhouses. Can also be used for solar powerplants were the intent of the receiver is to be used as a part of a sensible thermal energy storage system for concentrated solar power plants based upon the concept of storing solar heat in sand particles for a later discharge through a specific sand-steam heat exchanger. The results of the analysis indicate low-efficiency figures that can be caused by imperfections on the experimental setup and on the original design. Several paths of improvement are discussed in conclusion. ***Applications:*** * Concentrated solar power plants * Solar storage

1.4.1 Sand
Energy and Exergy Analysis of a Novel Gravity-fed Solid Particle Solar Receiver
An energy and exergy analysis of a novel solid particle solar receiver is presented based on experimental data and well-known correlations found in the literature. A sand sample from the deserts of the United Arab Emirates has been chosen as the solar absorber and heat carrier material. The intent of the receiver is to be used as a part of a sensible thermal energy storage system for concentrated solar power plants based upon the concept of storing solar heat in sand particles for a later discharge through a specific sand-steam heat exchanger. The results of the analysis indicate low efficiency figures that can be caused by imperfections on the experimental setup and on the original design. Several paths of improvement are discussed in conclusion.
05/01/2015 00:00:00
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1.4.2 Sand
Seasonal Solar Thermal Energy Sand-Bed Storage in a Region with Extended Freezing Periods: Part I Experimental Investigation
We present the first experimental study of sand-bed thermal energy storage conducted in a region with extended freezing period. The study was carried out on a home situated in Palmer, Alaska, 61.6° N, and 149.1° W. The home is equipped with evacuated tube solar thermal collectors that are connected to a seasonal sand-bed solar thermal energy storage system. Fourteen weeks of data was collected from a period of 28 January 2017 through 7 May 2017. Results suggest that seasonal sand-bed solar thermal storage systems are an excellent option for storing heat for climates in regions with long periods of freezing temperatures. The present study shows a proof of concept of a sand-bed seasonal solar thermal storage that needs additional controls for residential heating application. The system could also be used to provide heat for unoccupied spaces such as garages and greenhouses.
11/15/2017 00:00:00
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1.5 Solid industrial waste byproduct

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Within all the properties that define the suitability of a material to store sensible heat, waste materials stand out, especially for their low costs and availability. This heat recovery could be used for cogeneration, energy efficiency measures, passive heat recovery, solar cooling, etc. In this case, a solid by-product from the potash industry is tested in two different shapes to be used for industrial sensible heat recovery in high temperature, in a range of 100–200 °C. This heat recovery could be used for cogeneration, energy efficiency measures, passive heat recovery, solar cooling, etc. In this case, it is mostly made of NaCl. ***Applications:*** * Industrial heat

1.5.1 Solid industrial waste byproduct
Experimental characterization of a solid industrial by-product as material for high temperature sensible thermal energy storage (TES)
Nowadays, industrial processes use large quantities of fuel and electricity that produce heat, but much of which is wasted either to the atmosphere or to water. Many types of equipment have been developed to re-use some of this waste heat. Waste heat usefulness is determined by its temperature and its exergy; the higher the temperature the higher the quality or value. There are mainly three reversible methods to store it: sensible, latent and chemical. In this case, a solid by-product from the potash industry is tested in two different shapes to be used for industrial sensible heat recovery in high temperature, in a range of 100–200°C. This heat recovery could be used for cogeneration, energy efficiency measures, passive heat recovery, solar cooling, etc. Within all the properties that define the suitability of a material to store sensible heat, waste materials stand out especially for their low costs and availability. This heat recovery could be used for cogeneration, energy efficiency measures, passive heat recovery, solar cooling, etc. For that, a complete analysis of thermophysical properties was done both, at laboratory and a pilot plant scale. At the laboratory, the material composition was found to be NaCl as major phase. With differential scanning calorimetry (DSC) the specific heat capacity was determined as 0.738kJ/kg°C. The thermal stability was checked from ambient temperature to 800°C and the density and the conductivity at room temperature were also calculated. Also, a corrosion test was performed using samples of stainless steel at three degradation times, these results were compared with those obtained with Solar salt, a commercial and extended option for thermal energy storage (TES) applications at high temperature. At pilot plant scale, using 59kg of storage material, thermal cycles were performed with the storage material heating and cooling it from 100 to 200°C varying parameters as the heat transfer fluid (HTF) flow rate and the duration of the cycles.
01/01/2014 00:00:00
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2. Liquid sensible heat storage (L-SHS)

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Sensible heat storage systems utilize the heat capacity and the change in temperature of the material during the process of charging or discharging - temperature of the storage material rises when energy is absorbed and drops when energy is withdrawn. These techniques are based on liquids.


2.1 Aquifer Thermal Energy Storage (ATES)

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Aquifer thermal energy storage (ATES) is the storage and recovery of thermal energy in the subsurface. ATES is applied to provide heating and cooling to buildings. Storage and recovery of thermal energy are achieved by extraction and injection of groundwater from aquifers using groundwater wells. Systems commonly operate in a seasonal mode. The groundwater that is extracted in summer, is used for cooling by transferring heat from the building to the groundwater by means of a heat exchanger. Subsequently, the heated groundwater is injected back into the aquifer, which creates storage of heated groundwater. In wintertime, the flow direction is reversed such that the heated groundwater is extracted and can be used for heating (often in combination with a heat pump). Therefore, operating an ATES system uses the subsurface as a temporal storage to buffer seasonal variations in heating and cooling demand. When replacing traditional fossil-fuel dependent heating and cooling systems, ATES can serve as a cost-effective technology to reduce the primary energy consumption of a building and the associated CO₂ emissions. Some important parameters for an ATES installation are high ground porosity, medium to high hydraulic transmission rate around the boreholes, but a minimum of groundwater flow through the reservoir. Groundwater chemistry represents another set of parameters that must be given proper attention in order to prevent scale formation and furring. Numerous ATES facilities are in operation in Sweden, Germany, The Netherlands, Belgium, and some other European countries, including a system for heating and cooling at Oslo Hovedflyplass Gardermoen. The Netherlands is probably the technological leaders in the field. The efficiency of an aquifer in terms of storage and retrieval is around 70-90%. The cost of this storage method is 660-1100 euro/kW or approximately 22-33 euro/m³ (highly dependent on the size). The barriers for this method are the required site-specific hydrogeological conditions, relative lower energy density, lack of experience/ technical uncertainty and the requirements to balance the in and out of thermal energy to balance the aquifer. In the figure, the cost of four different water-based storage methods is shown. ***Applications:*** * Residential * Industrial

2.1.1 Aquifer Thermal Energy Storage (ATES)
Heating and cooling of a hospital using solar energy coupled with seasonal thermal energy storage in an aquifer
A system is being designed, using solar energy in combination with Aquifer Thermal Energy Storage (ATES), that will conserve a major part of the oil and electricity used for heating or cooling the Cukurova University, Balcali Hospital in Adana, Turkey. The general objective of the system is to provide heating and cooling to the hospital by storing solar heat underground in summer and cold in winter. As the main source of cold energy, ventilation air at the hospital and surface water from the nearby Seyhan Lake will be used.
01/01/2000 00:00:00
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2.1.2 Aquifer Thermal Energy Storage (ATES)
Productivity of Aquifer Thermal Energy Storage (ATES) in The Netherlands
Abstract Various forms of Aquifer Thermal Energy Storage (ATES) systems have been applied in The Netherlands. The systems differ with regard to the temperature at which the energy is stored, the type of energy supply system to which the storage belongs, and the type of user. The paper describes several different applications of ATES systems which may be used for heat storage, cold storage, and combined heat and cold storage. The productivity of these systems varies, and the payback period varies from 0 to 10 years. The paper compares cost-benefits for conventional and cold storage systems above and below ground, and reviews potential applications for industrial and commercial/institutional uses of ATES systems in The Netherlands.
01/01/1993 00:00:00
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2.2 Thermally (Vacuum) insulated water tank

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The solar heat energy is stored in a thermally insulated water tank and used in the heating period. The heat is also stored in the ground if necessary, using the ground loop of the heat pump if the water tank’s temperature rises above a certain threshold. If the temperature is too low for direct heating, then the heat pump can be used to extract the stored energy. This can also be performed under the form of a large subterranean buffer tank filled with water. Heat and cold can be added to or extracted from the tank through conductivity via its wall. The price of these systems is highly depended on the size, the price can vary from <1-165 euro/kWh. The storage efficiency of these systems is from 50-90%. ***Applications:*** * Residential * Agrifood * Heat Grids

2.2.1 Thermally (Vacuum) insulated water tank
De Reus van Schimmert : from a water tower to a green data center
The water tower of Schimmert is an iconic tower that has served the local community for decades. In 2014 it was decommissioned and currently local companies and authorities are searching for a viable business model for this imposing tower. The present report examines the feasibility of transforming the water tower into a data center that reuses its waste heat to provide sustainable heat to local residential and commercial consumers. The reservoir of the tower will be used for storage of the excess heat, in order to balance the mismatch between supply and demand. Data centers are the enablers of today’s digital society because they form the backbone of the internet infrastructure. As the demand of digital services increases, the energy demand and the corresponding environmental impact of the data center market intensifies. In addition to that, the servers housed in a data center generate heat during their operation and heat disposal is important in order to ensure a safe and reliable operation of the IT equipment. Although typically the waste heat is dissipated to the environment, there are ways of reusing it in order to improve the overall efficiency and provide a secondary source of income for the data center business. The proposed district heating system is one of these ways. The tower can be retrofitted into a data center of 450kW. The data center with a design PUE of 1.3 can be divided into 5 vertical compartments that will be built gradually as the IT load grows. In order to ensure uninterruptible operation, the proposed equipment resilience level is N+1 for all the systems, except for the power of the IT equipment where a 2N resilience is considered. The cooling method used for the servers has a significant impact on the quality of the waste heat and consequently on the ease of capturing it and reusing it. Although state of the art systems that use liquid or two-phase cooling show great potential, in this design air-cooled servers are proposed because of maintenance, reliability and flexibility reasons. To achieve the highest possible quality of the extracted heat a hot aisle containment is also suggested. The captured waste heat is enough to heat 65 houses in the vicinity of the tower in the village of Schimmert. The connection of the houses may take place in two phases, firstly the planned neighborhood of Bekerhof can connect to the heating grid and secondly houses that lay along the main piping system. Because the profiles of heat production of the data center and the heat demand of the heat clients are not balanced during operation, the reservoir of the water tower can be used as a heat storage system by storing any excess heat and covering any heat shortage. Water will be used as a storage medium since latent and thermochemical heat storage are still under development and have not been tested extensively in field applications. In addition to the technical investigation, this report provides an analysis of business opportunities for de Reus van Schimmert. There are a number of advantages for the selection of this tower for the proposed design, namely its location and the services already in place as well as the possible tax benefits and the durable design of the tower itself. The proposed company will be a cooperation between different stakeholders, a data center operator and a district heating operator. De Reus van Schimmert can be once again a lighting beacon of the area, this time because of its sustainable paradigm. It can showcase that although data centers demand massive amounts of electricity and as a consequence are responsible for CO2 emissions, they can put this energy in good use by providing sustainable heating to the local area.
01/01/2017 00:00:00
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2.2.2 Thermally (Vacuum) insulated water tank
Experimental investigations of the performance of a solar-ground source heat pump system operated in heating modes
Abstract Solar-ground source heat pump system (SGSHPS) is a new type of high efficiency, energy saving and environmental protection air-conditioning technology. In this paper, experimental studies and numerical simulation on the performance of a SGSHPS operated in different heating modes were carried out. The experimental system was installed in Nanjing of China and solar collectors were coupled with ground heat exchangers (GHE) through an insulated water tank. Four operation modes including ground source heat pump (GSHP), combined operation mode, day and night alternate operation mode and solar U-tube feeding heat alternate operation mode were investigated during winter season. The heat pump performance, solar collecting performance and borehole wall temperature variations were analyzed and compared for various modes. The experimental results indicate that for the combined operation mode, the system operation efficiency during day can be improved by the assistance of solar energy, and the excess solar energy collected during day can be stored in ground by the GHE to improve the operation performance of GSHP during night. The proportions of heat source burdened by solar and geothermal energy are 43.3% and 50.2% respectively. For the alternate operation modes, the temperature resumption of ground surrounding the GHE can be well achieved due to the intermittent heat extraction of GHE or feeding solar heat into ground and thus the overall utilization efficiency of solar and geothermal energy can be improved greatly. During the whole experimental period, the average COPs are 2.37 and 2.72 for GSHP and SAHP operation mode respectively, and the corresponding parameters are 2.69, 2.65 and 2.56 for the combined operation mode, day and night alternate operation mode and solar U-tube feeding heat alternate operation mode, respectively. The average solar collecting efficiency are 43.6%, 47.3% and 38.8% for the combined operation mode, SAHP operation mode and solar U-tube feeding heat operation mode, respectively. Based on the unit modeling, a dynamic simulation program was constructed to investigate the seasonal performance of the SGSHPS operated in different heating modes, the simulation results show that the seasonal average COP are 3.67, 3.64, 3.52 and 3.48 for the combined operation, day and night alternate operation, solar U-tube feeding heat and GSHP mode, respectively. From the view of improving the overall efficiency and increasing heat source fraction of solar energy, the combined operation mode is the best.
02/01/2015 00:00:00
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2.2.3 Thermally (Vacuum) insulated water tank
Increasing Solar Energy Usage for Dwelling Heating, Using Solar Collectors and Medium Sized Vacuum Insulated Storage Tank
This article describes a method for increasing the solar heat energy share in the heating of a dwelling. Solar irradiation is high in summer, in early autumn, and in spring, but during that same time, the heat demand of dwellings is low. This article describes a solution for storing solar heat energy in summertime as well as the calculations of the heat energy balance of such a storage system. The solar heat energy is stored in a thermally insulated water tank and used in the heating period. The heat is also stored in the ground if necessary, using the ground loop of the heat pump if the water tank’s temperature rises above a certain threshold. The stored heat energy is used directly for heating if the heat carrier temperature inside the tank is sufficient. If the temperature is too low for direct heating, then the heat pump can be used to extract the stored energy. The calculations are based on the solar irradiation measurements and heating demand data of a sample dwelling. The seasonal storing of solar heat energy can increase the solar heat energy usage and decrease the heat pump working time. The long-term storage tank capacity of 15 m 3 can increase the direct heating from solar by 41%. The direct heating system efficiency is 51%.
07/12/2018 00:00:00
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2.2.4 Thermally (Vacuum) insulated water tank
The multi-functional heat storage in Hamburg-Bramfeld - innovative extension of the oldest German solar energy housing estate
In 1996 the first large-scale seasonal solar thermal energy storage in Germany was built in Hamburg-Bramfeld. It was operated until 2009 in a central solar heating plant with seasonal storage storing solar thermal energy from the summer period to the heating season. The owner of the storage, the E.ON Hanse Warme GmbH, now decided to connect the storage to the district heating net of Hamburg-East and to convert it into an innovative multifunctional storage. This means that besides solar heat in future also surplus heat from a waste-fuelled cogeneration plant will be charged into the storage. With this connection a favourable combination of solar seasonal heat storage and waste heat from cogeneration will be demonstrated for the first time. The partners in this project are Hamburg Gas Consult GmbH for the design of the overall system, WTM Engineers GmbH for the design of the storage reconstruction, the Technical University of Brunswick (IGS) for monitoring and Solites for scientific accompaniment and advice.
01/01/2010 00:00:00
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2.3 Oils

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Thermal oils have the advantage that they act both as the heat transfer and the heat storage medium for medium to high-temperature domestic applications. These applications include steam generation and cooking of food. Although thermal oils are more expensive than water which is in abundance, the use of water in medium to high temperatures is limited by its boiling point. For small scale domestic applications which require non-sophisticated heat exchangers, thermal oils can be utilized. One of the first storage technologies consisted of accumulating hot oil in an insulated tank, with another tank for cold oil and for drawing from the hot oil, which becomes a heat reservoir. Another technique consists of using a tank of thermocline oil; the hot oil accumulating at the top of the tank, the cold at the bottom. The hot oil can then be pumped from the top of the tank as required. However, these two types of storage require a lot of oil which is very expensive. In addition, such an amount of oil can cause environmental problems in the event of accidental leakage. The developed storage beds subsequently have the advantage of considerably reducing the oil requirement in a thermal storage system. Different types of oil can be used for thermal storage, for example, Calorie HT 43 and Engine oil. Calorie HT43 is able to store from 12-260 °C and engine oil only up to 160 °C. Their ability capacity to store energy is; 1907 kJ/m³ K and 1670 kJ/m³ K. But, this is also highly depended on the temperature used for oils. ***Applications:*** * Solar cookers * Automotive * Solar thermoelectric applications * Domestic scale oil tank

2.3.1 Oils
Experimental investigation of the solar cooker during sunshine and off-sunshine hours using the thermal energy storage unit based on a parabolic trough collector
A solar cooker based on a parabolic trough collector with thermal energy storage (TES) was investigated. In this experimental set-up, solar radiations were focused on the absorber tube and the collected heat was transferred to the solar cooker by natural circulation (thermosiphon) of the working fluid. The water and thermal oil (engine oil) were used separately as working fluids. Acetanilide was used as the TES material in the solar cooker. In day time, the phase change material (PCM) stored heat as well as transferred it to the cooking pot. In evening time, the stored energy by PCM was used to cook the food. The cooking process was carried out with different foods and with variation in the quantity of food. It was found that the temperature of thermal oil was 10–24°C higher than water as the working fluid. The system was able to cook the food twice a day and the rate of evening cooking was higher as compared with noon cooking. Using thermal oil as the working fluid, the quantity of heat stored by PCM was...
11/01/2016 00:00:00
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2.3.2 Oils
High temperature latent heat thermal energy storage: Phase change materials, design considerations and performance enhancement techniques
A very common problem in solar power generation plants and various other industrial processes is the existing gap between the period of thermal energy availability and its period of usage. This situation creates the need for an effective method by which excess heat can be stored for later use. Latent heat thermal energy storage is one of the most efficient ways of storing thermal energy through which the disparity between energy production or availability and consumption can be corrected, thus avoiding wastage and increasing the process efficiency.
11/01/2013 00:00:00
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2.3.3 Oils
Investigating the Effect of Different Heat Storage Media on the Thermal Performances of Double Exposure Box-type Solar Cookers
This paper investigates the effect of some heat storage materials on the thermal performances of double exposure box-type solar cookers. Benzoic acid, stearic acid and vegetable oil were used in storing heat in double exposure box-type solar cookers. Using standard methods, some thermal performance parameters were evaluated and compared to a control design (no heat storage). The average first figure of merit were; 0.13, 0.14, 0.12 and 0.11 ℃ m-2 W-1 for benzoic acid, control, stearic acid and vegetable oil cookers, respectively, while their respective second figure of merit were; 0.45, 0.40, 0.10 and 0.12. Benzoic acid influenced a higher thermal performance while stearic acid and vegetable oil had a reduction effect. Benzoic acid and vegetable oil had significant effect on the cooking power of the solar cookers while stearic acid had effect on the first figure of merit.
09/06/2016 00:00:00
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2.3.4 Oils
Performance comparison of thermal energy storage oils for solar cookers during charging
Charging experiments to evaluate the thermal performance of three thermal energy storage oils for solar cookers are presented. An experimental setup using an insulated 20 L storage tank is used to perform the experiments. The three thermal oils evaluated are Sunflower Oil, Shell Thermia C and Shell Thermia B. Energy and exergy based thermal performance parameters are evaluated. A new parameter, the exergy factor, is proposed which evaluates the ratio of the exergy content to the energy content. Sunflower Oil performs better than the other thermal oils under high power charging. Thermal performances of the oils are comparable under low power charging.
12/01/2014 00:00:00
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2.4 Molten Salts

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Molten salts can be employed as a thermal energy storage method to retain thermal energy. Presently, this is a commercially used technology to store the heat collected by concentrated solar power (e.g., from a solar tower or solar trough). The heat can later be converted into superheated steam to power conventional steam turbines and generate electricity in bad weather or at night. The salt melts at 131 °C. It is kept in the liquid state at 288 °C in an insulated "cold" storage tank. The liquid salt is pumped through panels in a solar collector where the focused sun heats it to 566 °C. It is then sent to a hot storage tank. With proper insulation of the tank the thermal energy can be usefully stored for up to a week. When electricity is needed, the hot molten salt is pumped to a conventional steam-generator to produce superheated steam for driving a conventional turbine/generator set as used in any coal or oil or nuclear power plant. Different existing concept and salts: Two tanks / One tank storage using NaNO₃/ KNO₃ / Ca(NO₃)₂ ***Applications:*** * Concentrated solar power plants

2.4.1 Molten Salts
Long term thermal energy storage with stable supercooled sodium acetate trihydrate
Abstract Utilizing stable supercooling of sodium acetate trihydrate makes it possible to store thermal energy partly loss free. This principle makes seasonal heat storage in compact systems possible. To keep high and stable energy content and cycling stability phase separation of the storage material must be avoided. This can be done by the use of the thickening agents carboxymethyl cellulose or xanthan rubber. Stable supercooling requires that the sodium acetate trihydrate is heated to a temperature somewhat higher than the melting temperature of 58 °C before it cools down. As the phase change material melts it expands and will cause a pressure built up in a closed chamber which might compromise stability of the supercooling. This can be avoided by having an air volume above the phase change material connected to an external pressure less expansion tank. Supercooled sodium acetate trihydrate at 20 °C stores up to 230 kJ/kg. TRNSYS simulations of a solar combi system including a storage with four heat storage modules of each 200 kg of sodium acetate trihydrate utilizing stable supercooling achieved a solar fraction of 80% for a low energy house in Danish climatic conditions.
12/01/2015 00:00:00
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2.4.2 Molten Salts
Molten salt heat storage material
The invention relates to an medium temperature molten salt energy storage technology, and heat is stored by means of molten salt. The invention particularly relates to the molten salt and a preparation method thereof. The molten salt is prepared from sodium nitrate, sodium nitrite and sodium hydroxide. The molten salt preparation method comprises the following steps that sodium nitrate, sodium nitrite and sodium hydroxide are mixed with graphite according to certain mass, under the condition of 200-400 DEG C, heating is conducted for 1-7 hours, then cooling is conducted to reach the room temperature, and the molten salt is obtained. The molten salt is high in stability, high in latent heat, high in heat storage density and low in price; the technology for preparing the molten salt is simple, convenience is brought to production, safety and reliability are achieved, standardization of molten salt preparation can be achieved, the technology is suitable for large-scale industrial production, and emission of three wastes does not exist.
08/31/2018 00:00:00
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2.4.3 Molten Salts
Review on concentrating solar power plants and new developments in high temperature thermal energy storage technologies
A concentrating solar power (CSP) system converts sunlight into a heat source which can be used to drive a conventional power plant. Thermal energy storage (TES) improves the dispatchability of a CSP plant. Heat can be stored in either sensible, latent or thermochemical storage. Commercial deployment of CSP systems have been achieved in recent years with the two-tank sensible storage system using molten salt as the storage medium. Considerable research effort has been conducted to improve the efficiency of the CSP system and make the cost of electricity comparable to that of the conventional fossil-fuel power plant. This paper provides a comprehensive summary of CSP plants both in operation and under construction. It covers the available technologies for the receiver, thermal storage, power block and heat transfer fluid. This paper also reviews developments in high temperature TES over the past decade with a focus on sensible and latent heat storage. High temperature corrosion and economic aspects of these systems are also discussed.
01/01/2016 00:00:00
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2.5 Heat and ground pumped hydro energy storage

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Using compressed water system to store heat. A startup and a research project have been found on this topic. No direct suppliers * GLIDES: A novel Ground-Level Integrated Diverse Energy Storage (GLIDES) system which can store energy via an input of electricity or heat and deliver dispatchable electricity. The proposed system is lowcost and hybridizes compressed air and pumped storage approaches that will allow for the offpeak storage of intermittent renewable energy for use during peak times. GLIDES stores electricity mechanically in the form of compressed gas that displaces water in high-pressure vessels. * Isentropic: PHES Thermal Stores are split into layers to achieve high efficiency of thermal transfer, low-pressure drop and higher energy density than other 'packed bed' stores. The PHES Thermal Stores work by direct heat exchange between high-pressure gas and particles of crushed rock or gravel. It will be a stand-alone energy storage system called Pumped Heat Energy Storage (PHES). The cycle uses a proprietary reciprocating heat pump/engine (developed in-house). It will take electricity from the grid to charge the system. ***Applications:*** * Small industry * Residential

2.5.1 Heat and ground pumped hydro energy storage
Experimental and analytical evaluation of a hydro-pneumatic compressed-air Ground-Level Integrated Diverse Energy Storage (GLIDES) system
Abstract In recent times, there has been a significant increase in intermittent renewable electricity capacity additions to the generation mix. This, coupled with an aging electrical grid that is poorly equipped to handle the ensuing mismatch between generation and use, has created a strong need for flexible, advanced bulk energy storage technologies. In this paper, one such technology recently invented and demonstrated at Oak Ridge National Laboratory is introduced and characterized. Similar to compressed-air energy storage, the Ground-Level Integrated Diverse Energy Storage (GLIDES) technology is based on gas compression/expansion, however, liquid-piston compression and expansion are utilized. In common with pumped-storage hydroelectricity, hydraulic turbomachines (pump/turbine) are utilized for energy storage and recovery, however, pressure vessels are utilized to create artificial elevation (head) difference, allowing pressure head of several thousands of feet to be reached. This paper reports on the experimental performance of the first GLIDES proof-of-concept prototype, and presents formulation and results from a validated physics-based simulation model.
07/01/2018 00:00:00
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2.5.2 Heat and ground pumped hydro energy storage
GLIDES – Efficient Energy Storage from ORNL
The research shown in this video features the GLIDES (Ground-Level Integrated Diverse Energy Storage) project, which has been under development at Oak Ridge National Laboratory (ORNL) since 2013. GLIDES can store energy via combined inputs of electricity and heat, and deliver dispatchable electricity. Supported by ORNL’s Laboratory Director’s Research and Development (LDRD) fund, this energy storage system is low-cost, and hybridizes compressed air and pumped-hydro approaches to allow for storage of intermittent renewable energy at high efficiency. A U.S. patent application for this novel energy storage concept has been submitted, and research findings suggest it has the potential to be a flexible, low-cost, scalable, high-efficiency option for energy storage, especially useful in residential and commercial buildings.
03/01/2016 00:00:00
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2.5.3 Heat and ground pumped hydro energy storage
Transient Thermofluids Analysis of a Ground-Level Integrated Diverse Energy Storage (GLIDES) System
In this work, a novel Ground-Level Integrated Diverse Energy Storage (GLIDES) system which can store energy via input of electricity or heat and deliver dispatchable electricity is presented [1]. The proposed system is low-cost and hybridizes compressed air and pumped-storage approaches that will allow for the off-peak storage of intermittent renewable energy for use during peak times. A detailed control-volume energy analysis of the system is carried out, yielding a set of coupled differential equations which are discretized using a finite difference scheme and used to model the transient response during charging and discharging. The energy analysis includes coupled heat transfer and pressure drop analysis used to predict system losses for more accurate round trip efficiency (RTE) calculations and specific energy density (ED) predictions. Preliminary analysis of the current prototype indicates an electric-to-electric RTEE of 66% (corresponding to shaft-to-shaft mechanical RTEM of 78%) and ED of 2.5 MJ/m3 of air, given initial air volume and pressure of 2 m3 and 70 bar. The electric power output ranges from a max of 2.5 kW to a min of 1.2 kW and the output current ranges from a max of approximately 21 amps to approximately 10 amps at 120 V, 60 Hz dispatchable electricity, over a period of approximately 50 minutes. Additionally, it is shown that heat transfer enhancement to the point of a 5-fold increase in air heat transfer rates results in a near 5% improvement in RTEE (70% considering all component losses). Additional component efficiency improvements and efficiency gains due to system scale-up could see higher achievable RTEs.Copyright © 2015 by ASME
11/13/2015 00:00:00
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3. Mix of solid - liquid sensible heat (SL-SHS)

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Mix of liquid and solid heat storage


3.1 Borehole thermal energy storage (Soil storage)

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Borehole thermal energy storage (BTES) system is an underground structure for storing large quantities of solar heat collected in summer for use later in winter. It is basically a large, underground heat exchanger. To Store solar energy in the soil under and near the building. In unsaturated soil or in rock the most interesting techniques are heat exchangers in vertical boreholes. Via these heat exchangers, the energy is transferred to the ground which serves as heat capacity and is heated up to the required temperatures. Depending on the temperature level, the thermal energy is, extracted either by a heat pump (low-temperature ground storage, 0°C-40°C) or directly (high-temperature ground storage, 40°C-80°C) and delivered to the consumers. As a result of the limited thermal conductivity, the heat losses are rather moderate and storage efficiencies of 70% can be reached. In contrast, good thermal contact between the heat exchangers and the ground is required to allow a good heat transfer rate per unit area of the heat exchanger tube. In unconsolidated soils like clay, silt, or sand, heat capacity and thermal conductivity are strongly dependent on the water content especially at higher temperatures (> 60°C). In this region, water losses can occur because of vapour diffusion along the temperature gradient which can lead to dry-out and cracking in the area surrounding the heat exchanger tubes in the worst The capital cost of a large Borehole thermal energy storage system can be significant, as a large number of geothermal boreholes will need to be drilled, compared to just a few thermal wells for an ATES system. However, the installation cost should be similar to conventional GSHP systems, and the higher COP values will result in a lower total life-cycle cost than a conventional GSHP system. Both closed-loop geothermal systems will have a lower life-cycle cost than a conventional fossil-fuel-fired HVAC system. Because BTES is a closed-loop geothermal technology, there should be little difficulty in obtaining permits. Typically, the most common constraint is on the available land area in which to construct the GHX array. Because of their construction principle, BTES are not thermally insulated to the bottom and the side, only a top insulation layer reduces the losses to the environment. As the thermal conductivity of underground material is rather moderate, in a range of 1–5 W/mK, heat losses can be kept low if the total volume is large enough to achieve a good surface-to-volume ratio. Size is important because heat losses are proportional to the storage surface while the storage capacity is proportional to the volume. The efficiency of a borehole is estimated from 6-54 %, which increases the longer the system is into use. Therefore BTES are typically large and thus contain a high storage capacity. Additionally, BTES construction can be relatively cheap, even to a high quality, which allows its use even from an economical point of view for seasonal storage with 1–2 storage cycles per year. The cost estimations of a BTES are estimated around 0.3-3.3 €/kWh or 11-50 €/m³ depending on the size and the method for measuring the retained heat in the ground. The temperature across the ThermalBank can be increased from its natural temperature of 10°C to over 25°C in the course of the summer months. Current barriers are limited charging and discharging capabilities, geological constraints, avoiding of groundwater, the number of utilities is limited, technical uncertainty, low-temperature storage and the system usually requires a buffer tank. ***Applications:*** * District/Residential * Industrial

3.1.1 Borehole thermal energy storage (Soil storage)
Analysis of an integrated heating and cooling system for a building complex with focus on long–term thermal storage
Abstract Modern building complexes have simultaneous heating and cooling demands. Therefore, integrated energy systems with heat pumps and long-term thermal storage are a promising solution. An integrated heating and cooling system for a building complex in Oslo, Norway was analyzed in this study. The main components of the system were heat pumps, solar thermal collectors, storage tanks, ice thermal energy storage, and borehole thermal energy storage. Dynamic simulation models were developed in Modelica with focus on the long-term thermal energy storage. One year measurement data was used to calibrate the system model and two COPs were defined to evaluate system performance. The simulation results showed that more heat had to be extracted from the long-term thermal storage during winter than could be injected during summer. This imbalance led to a decrease in ground temperature (3 °C after 5 years) and decreasing long-term performance of the system: both COPs decreased by 10% within five years. This performance decrease could be avoided by increasing the number of solar collectors from 140 to 830 or by importing more heat from the local district heating system. Both measures led to sustainable operation with a balanced long-term thermal storage.
12/01/2018 00:00:00
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3.1.2 Borehole thermal energy storage (Soil storage)
Comparison of Modelled Distribution of Thermal Fields at Seasonal Ground Storage Segments
In order to reduce the energy demand leads to the creation of alternative ways, how to store energy for extended time period and cover starting part of winter term with heating. One possibly way is to store solar energy in the soil under and near the building. This article focuses on comparing the distribution and thermal unsteady field in the seasonal distribution elements of the ground storage located under the building. The comparison will occurred change of accumulated material properties and optimal distance distribution pipes or elements, so as to create the most efficient storing systems.
02/01/2014 00:00:00
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3.1.3 Borehole thermal energy storage (Soil storage)
Control and Monitoring of a BTES-System
Thermal energy produced from solar collectors can be stored in Borehole Thermal Energy Storage, BTES, when demand is low for later usage when demand is high. The aim of this thesis is to develop a scalable system architecture for control and monitoring of a BTES prototype.The BTES prototype consist of 13 boreholes configured in a hierarchically manner in two circles and one core. The core is of the highest priority. The operational information is displayed on a website and stored in a database.The data communication consist of two One-wire buses and one CAN bus. The temperature sensors are connected to the One-Wire buses. The CAN bus consist of sensor/actuator nodes and a server node. Based on sensor data, a control loop configures the actuators. Operational data is stored in a database and visually presented on a website. The website displays an overview of all the boreholes where all of the sensors data can be read. The control algorithm runs successfully according to its hierarchically priorities. The prototype works as a developement platform and a demonstrating prototype.
01/01/2016 00:00:00
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3.1.4 Borehole thermal energy storage (Soil storage)
Effects of the District Heating Supply Temperature on the Efficiency of Borehole Thermal Energy Storage Systems
The mismatch of high heat demand in winter and high solar heat supply in summer can be compensated by solar district heating (SDH) with borehole thermal energy storage (BTES) systems. Transient simulations are imperative to attain a good understanding of the system behavior and to determine an optimized system design. In this context, the models of SDH systems and BTES pose very different requirements on their simulation environments. Taking this into account, a coupled simulation, in which both models can be realized in separate and specialized simulation environments becomes favorable. In the presented work, a SDH modeled in SimulationX (Modelica) and a BTES modeled in FEFLOW (Finite Element subsurface FLOW system) were simulated simultaneously and coupled via a TCP/IP connection. An adaptive communication step size control was implemented, to minimize both the error in transmitted energy and the computational effort. Recent studies have shown that the performances of the single components of SDH with integrated BTES – and thus the whole system – strongly depend on design parameters like size, system architecture and control strategy. With the aforementioned method the strong interdependencies and the complex system behavior can be simulated in high detail, which allows for a comprehensive analysis and subsequent identification of energetic inefficiencies. The temperature level of the district heating flow proves to be a parameter, which has a strong effect on the storage performance as well as on the system efficiency. A case study is carried out, to illustrate the difference in efficiency of BTES integrated into district heating grids with different flow temperatures. It analyzes the potentials of an integration of a BTES into the existing district heating grid of the TU Darmstadt with and without a reduction of the grid flow temperature. During summer, a solar thermal collector field and buffer storages are used to the charge of the BTES system, whereas a heat pump was added for discharging it in winter. The results support the general opinion that low district heating flow temperatures and respectively low return temperatures are crucial for an efficient operation of SDH systems with integrated BTES. The storage, the solar thermal collectors and the heat pump can be operated in an energetically much more favorable way. As a consequence it can be said that not only district heating systems profit from the integration of seasonal BTES, but the efficient operation of the storage itself is highly dependent on the shift to 4th generation district heating.
09/18/2017 00:00:00
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3.1.5 Borehole thermal energy storage (Soil storage)
Ground Thermal Responses During Heat Exchange at EcoFarm
This paper analyzes the ground thermal responses during constant rate of heat injection and extraction. The undisturbed underground temperature is assumed to be uniform. Seven types of earth material are analyzed using mean values of their thermal properties. Simple equation for Zone of Influence, convenient for quick engineering assessment, is derived. The results show that, among seven underground materials studied, dry sand and sand aquifer are the best for storage type application of thermal energy; whereas igneous is the best for dissipative type application of geothermal energy. ne of the solutions to fulfill household energy demands without using fossil fuel resources is to exchange heat with the ground by means of a Borehole Heat Exchanger (BHE). The objective of the applications is to use the natural ground temperature as a heat source during the heating mode and as a recipient of heat during the cooling mode. The ensuing change of ground temperature change around the boreholes should be kept small in order to avoid reduced performance of the system. A maximum thermal interaction with the surrounding ground is desired in BHE application, since the intention is to dissipate the thermal energy in the ground. In severely cold regions like Canada where heating requirement is much higher than that of cooling, an auxiliary heat source must be used to avert annual energy imbalance and to improve efficiency of heat pump in heating season. The ground is used for storage of thermal energy, by means of Borehole Thermal Energy Storage (BTES) system. In such cases, the thermal interaction with the ground surrounding the storage volume is undesirable. Solar energy, a green and renewable energy, could be an ideal auxiliary energy source for such system (1). In both dissipative and storage type applications, fundamental understanding of thermal response of ground to heat injection/extraction is essential to achieve cost-effective designs of BHE and BTES systems. To the author's knowledge, characteristics of temperature response for different layers of underground soil/bedrock material have not been studied intently. This paper presents thermal response of soils and rocks subjected to heat injection and extraction, and its design implications to BHE and BTES systems either already existing or to be installed at EcoFarm, Caledon, Canada. The undisturbed underground temperature is assumed to be uniform.
05/01/2013 00:00:00
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3.1.6 Borehole thermal energy storage (Soil storage)
Impact of coupled heat transfer and water flow on soil borehole thermal energy storage (SBTES) systems: Experimental and modeling investigation
Abstract A promising energy storage option is to inject and store heat generated from renewable energy sources in geothermal borehole arrays to form soil-borehole thermal energy storage (SBTES) systems. Although it is widely recognized that the movement of water in liquid and vapor forms through unsaturated soils is closely coupled to heat transfer, these coupled processes have not been considered in modeling of SBTES systems located in the vadose zone. Instead, previous analyses have assumed that the soil is a purely conductive medium with constant hydraulic and thermal properties. Numerical modeling tools that are available to consider these coupled processes have not been applied to SBTES systems partly due to the scarcity of field or laboratory data needed for validation. The goal of this work is to test different conceptual and mathematical formulations that are used in heat and mass transfer theories and determine their importance in modeling SBTES systems. First, a non-isothermal numerical model that simulates coupled heat, water vapor and liquid water flux through soil and considers non-equilibrium liquid/gas phase change was adopted to simulate SBTES systems. Next, this model was used to investigate different coupled heat transfer and water flow using nonisothermal hydraulic and thermal constitutive models. Data collected from laboratory-scale tank tests involving heating of an unsaturated sand layer were used to validate the numerical simulations. Results demonstrate the need to include thermally induced water flow in modeling efforts as well as convective heat transfer, especially when modeling unsaturated flow systems. For the boundary conditions and soil types considered, convective heat flux arising from thermally induced water flow was greater than heat transfer due to conductive heat flux alone. Although this analysis needs to be applied to the geometry and site conditions for SBTES systems in the vadose zone, this observation indicates that thermally induced water flow can have significant effects on the efficiency of heat injection and extraction.
09/01/2015 00:00:00
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3.1.7 Borehole thermal energy storage (Soil storage)
Improvement of Borehole Thermal Energy Storage Design Based on Experimental and Modelling Results
Underground Thermal Energy Storage appears to be an attractive solution for solar thermal energy storage. The SOLARGEOTHERM research project aimed to evaluate the energetic potential of borehole thermal energy storage by means of a full-scale experimental device and heat transfer models. Analysis of the experimental data showed that a single borehole is not efficient for storage. Models showed that the heat transfer fluid in the geothermal probe lost 15 per cent of its energy at a depth of 100 m and 25 per cent at 150 m. A relation was established that enables comparison of the storage characteristic time of any vertical BTES to an optimum one. Finally, guidelines are formulated to optimise the design of vertical borehole fields with an objective of inter-seasonal heat storage.
07/01/2014 00:00:00
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3.1.8 Borehole thermal energy storage (Soil storage)
Life Cycle Analysis of Underground Thermal Energy Storage
Underground Thermal Energy Storage (UTES) systems are used to buffer the seasonal difference between heat and cold supply and demand and, therefore, represent an interesting option to conserve energy. Even though UTES are considered environmental friendly solutions they are not completely free of impacts on the environment in general and the subsurface in particular. In order to improve the understanding and knowledge on the environmental performance of UTES techniques, this study performed a Life Cycle Assessment (LCA) on two different UTES systems: Aquifer Thermal Energy Storage (ATES) and Borehole Thermal Energy Storage (BTES).
01/01/2015 00:00:00
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3.1.9 Borehole thermal energy storage (Soil storage)
Low temp. waste heat utilisation - uses ground heat, earth heat storage ability and deep long term storage
The system utilises and stores low temp. waste heat from power stations and industrial plants. The heat may be used directly, or after further heating by heat pumps, to heat rooms and water, esp. in multi-storey buildings, and swimming pools. Excess heat, and any other waste heat, is stored in a storage medium at great depth, or in the ground itself. When withdrawing heat, the medium is cooled to below its freezing point, utilising any latent heat, and heat is withdrawn from the surrounding ground, which is at a higher temp. After withdrawal, the storage medium is heated by warmth from the ground and solar radiation. Excess heat from the rooms is fed via a cooling system into a long term store.
09/17/1981 00:00:00
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3.1.10 Borehole thermal energy storage (Soil storage)
Modelling of the thermal performance of a borehole field containing a large buried tank
Abstract Seasonal storage of solar thermal energy for space heating of multiple dwellings in cold climates can be accomplished through the use of borehole fields in conjunction with large buffer tanks. The buffer tank is used to account for the difference between the time over which solar energy can be collected and the time required to deposit the collected energy into the borehole field. There is motivation to bury the tanks in order to save space on ground level, as well as to improve the overall efficiency of the system by reducing heat losses from the tank. The current paper uses computational fluid dynamics (CFD) to explore the impact of a buried tank on the performance of a borehole thermal energy storage (BTES), as well as the thermal interactions between the tank and boreholes. The long-term performance was assessed in detail by simulating a 20-year period. The first 5 years of performance were then compared to results for a series of other cases including: a typical BTES layout, a tank with the bottom wall insulated as well as tanks with varying aspect ratios. It was found that the presence of the tank did not significantly reduce the BTES performance. Moreover, performance was relatively insensitive to the tank aspect ratio. Insulating the bottom of the tank also had negligible difference.
03/01/2016 00:00:00
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3.1.11 Borehole thermal energy storage (Soil storage)
Performance analysis of a soil-based thermal energy storage system using solar-driven air-source heat pump for Danish buildings sector
Abstract Denmark has set an ambitious long-term future energy goal to become independent of fossil fuel by 2050, depending completely on renewable and alternative resources in the energy and transport sectors. Solar energy is one of the most favourable alternative resources in terms of cleanness, safety and the economic and environmental aspects. However, the intermittent nature of solar energy and the lack of high solar radiation intensities in various climates favour the use of various energy storage techniques to eliminate the discrepancy between energy supply and demand. The current work presents an analysis and evaluation of the performance of an underground soil-based thermal energy storage system for solar energy storage, coupled with a combined heat and power generation system. A combined PV-Air Source Heat Pump (ASHP) system is utilized to fulfil heating and electricity needs of a housing project in Odense, Denmark, in addition to charging the soil storage medium in summer months when excess electric power is generated. The stored heat is discharged in December and January to provide the space heating and domestic hot water demands of the residential project without the utilization of an external heating source. Employing a PV system of 30 kW capacity, it was found that a storage medium of 900 m 3 of soil is capable of providing the heating needs for a housing project of 1000 m 2 internal floor area. The year round transient behaviour of the thermal energy storage medium is reported in addition to the heat losses and the surrounding soil temperature variation throughout the year. It was found that the overall system heating coefficient of performance is around 4.76, where the reported energetic efficiency is 5.88% for the standalone PV system, 19.1% for the combined PV-ASHP system, and 22.2% for the combined PV-ASHP system employing a seasonal underground thermal energy storage block.
03/01/2017 00:00:00
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3.1.12 Borehole thermal energy storage (Soil storage)
Seasonal Low Temperature Borehole Thermal Energy Storage - Utilizing excess heat for district heating in Gothenburg.
Occasionally during summer the heat load in the district heating (DH) network of the Gothenburg region exceeds the heat demand of the customer, i.e. there is an excess of heat in the DH-network. Nowadays, this excess heat is cooled against a river or in a cooling tower at a waste incineration plant. The aim of this study is to store this excess heat in the ground instead of cooling it against a river and use this excess heat during occasions when the heating demand is higher, during winter. This excess heat will be stored in a borehole thermal energy storage (BTES). The studied BTES will be connected to existing heat pumps at Ryaverket owned by Goteborg Energi AB. The conditions, regarding temperature and volumetric ow rate, of the heat source of the heat pumps, treated sewage water, will be improved with the aid of a BTES. When these previously mentioned conditions of the sewage water are improved more heat can be generated by the heat pumps. An increased heat generation by the heat pumps will replace heat generated by other, more expensive, heat generation units. To evaluate the economic profitability of such a system the net present value has been calculated. Designs for BTES, storing 50GWh and 25GWh of waste heat, are found with the aid of a software named GLHEpro and the investment cost for these designs are calculated. To reach economic profitability for this project the savings made by this new system,when heat generated by the heat pumps is increased, should meet the extent of the investment cost. To be able to calculate the savings, a software named Martes is used. The investment cost of a BTES is ten times larger than the savings ever will be in the most probable scenario regarding the investment cost of a BTES. Economic profitability is only reached if the investment cost of the BTES is in the minimum price range, if subsidies to cover 40% of the investment cost from Horizon2020 is gained, if an interest rate of 5% is used for economic calculations and when the availability of the heat pumps is increased by 15%. Economic profitability can also be gained for a scenario when the prices for the investment cost are in the minimum price range and an interest rate of 0% is used for economic calculations. It seems rather unlikely to gain all these privileges for this case study to become economically profitable.
01/01/2015 00:00:00
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3.1.13 Borehole thermal energy storage (Soil storage)
Seasonal Thermal-Energy Storage: A Critical Review on BTES Systems, Modeling, and System Design for Higher System Efficiency
Buildings consume approximately ¾ of the total electricity generated in the United States, contributing significantly to fossil fuel emissions. Sustainable and renewable energy production can reduce fossil fuel use, but necessitates storage for energy reliability in order to compensate for the intermittency of renewable energy generation. Energy storage is critical for success in developing a sustainable energy grid because it facilitates higher renewable energy penetration by mitigating the gap between energy generation and demand. This review analyzes recent case studies—numerical and field experiments—seen by borehole thermal energy storage (BTES) in space heating and domestic hot water capacities, coupled with solar thermal energy. System design, model development, and working principle(s) are the primary focus of this analysis. A synopsis of the current efforts to effectively model BTES is presented as well. The literature review reveals that: (1) energy storage is most effective when diurnal and seasonal storage are used in conjunction; (2) no established link exists between BTES computational fluid dynamics (CFD) models integrated with whole building energy analysis tools, rather than parameter-fit component models; (3) BTES has less geographical limitations than Aquifer Thermal Energy Storage (ATES) and lower installation cost scale than hot water tanks and (4) BTES is more often used for heating than for cooling applications.
05/25/2017 00:00:00
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3.1.14 Borehole thermal energy storage (Soil storage)
Solar community heating and cooling system with borehole thermal energy storage – Review of systems
There is a substantial need to accelerate the advancement and implementation of advanced clean energy technologies to solve challenges of the energy crisis, climate change, and sustainable processes. Solar heating and cooling technologies are feasible solutions among clean energy technologies. This paper presents a detailed literature review on studies performed around the solar district energy systems with integrated thermal storage. They are mainly either for heating or cooling. The combined district heating and cooling system with both systems integrated with borehole thermal energy storage (BTES) has not been fully explored. A low-temperature distribution fluid, suitable for use in distributed heat pumps around the community with BTES, has also not been practically installed yet. Such system, could reduce the transmission/distribution heat loss within the community, and lower the required amount of energy production and storage, compared to the other systems. This could make the entire system techno-economically more attractive while not compromising energy efficiency of the system.
07/01/2016 00:00:00
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3.1.15 Borehole thermal energy storage (Soil storage)
The Effectiveness of Borehole Heat Exchanger Depth on Heat Transfer Rate, Study with Numerical Method Using a CFD 3D Simulation
Excess solar thermal energy is available, while in winter, when thermal energy is needed for heating systems, its quantity is usually not sufficient. There are different options to cope with the seasonal offset of thermal energy supply and demand. One of these options is borehole thermal energy storages (BTES). Borehole thermal energy storages coupled with ground source heat pumps have been widely developed and researched. The major disadvantage of (BTES) is the initial capital cost required to drill the boreholes. Geothermal energy piles were developed to help offset the high initial cost of these systems. This study investigates thermal performance of vertical ground heat exchangers with constant inlet water temperatures and deferent borehole depths. The performances of three models of U-tube with depth of 100m, 60m, and 30m are evaluated by numerical method using a CFD 3D simulation. The simulation results show that heat transfer rates decrease in the heating mode for 100m depth, and show that the best borehole depth regarding to heat transfer rate efficiency is 60m depth borehole. However for heat storage capacity the model of 100m depth is the best. The results show that increasing the depth of borehole heat exchangers lower the heat exchange efficiency with the ground. By comparing with 100 m depth, the heat transfer rates per unit borehole depth lower of 3.1% in 60 m depth. According to all results, it is highly recommended to construct medium depth around 60 m depth of borehole with U-shaped pipe configuration, due to higher efficiency in heat transfer rate.
10/30/2018 00:00:00
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3.1.16 Borehole thermal energy storage (Soil storage)
Thermoeconomic Design of Borehole Thermal Energy Storage Systems
Borehole thermal energy storage (BTES) is an option to provide large-scale seasonal storage of cold and heat in natural underground sites. Boreholes are used to transfer heat from the working fluid to the ground in charging phase and vice versa in discharging.The design of boreholes influences system efficiency, installation costs and the charging time required to reach the design temperature in the ground. The latter can result too long but may be reduced significantly through the selection of an optimal design and a storage temperature that maximizes the efficiency. Nevertheless high performances are usually accompanied by high purchase and installation costs of the borehole exchangers. The increase in efficiency and the decrease of investment costs are two conflicting objectives that must be considered in the design stage to select the best configuration.This work is focused on the optimal configuration of BTES in which the boreholes are used to charge the ground to the design temperature and to supply the thermal energy demand during the operation. Several designs are explored at two different levels of temperature in the storage.A novel design strategy, based on energy, exergy and thermoeconomic analysis, is proposed to select the optimal configuration that guarantees a balance between expenditure on capital costs and exergy efficiency. This constitutes a novel approach which ensures high performances of BTES systems for long periods of operation, which is an interesting area of research that is currently not sufficiently explored.Copyright © 2015 by ASME
11/13/2015 00:00:00
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4. Solid-solid latent heat storage (SS-LHS)

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Solid-solid phase change materials(SS-PCMs) absorb and release heat by reversible phase transitions between a (solid) crystalline or semi-crystalline phase, and another (solid) amorphous,semi-crystalline, or crystalline phase. Different from solid-liquid-PCMs, solid-solid-PCMs retain their bulk solid properties within certain temperature ranges and are therefore also referred to as ‘‘solid-state” PCMs. In general PCM materials have specific energy within the range of 50-150 kWh/t with an energy capacity of 100 kWh/m³. The efficiency of these systems is around 75-90% and storage periods are mostly hour-week based. The power which can be retrieved from these systems is around 0.001-1 MW depending on the size. The cost of the PCM is around 10-50 €/kWh. General advantages of latent heat storage: * Higher energy density compared to sensible heat storage * Energy can be provided at an almost constant temperature General disadvantages of latent heat storage: * Lack of thermal stability of materials/degradation problems * Cost of materials van be high * Corrosive materials * Low thermal conductivity


4.1 Inorganic

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Inorganic SS-PCMs are able to store/release thermal energy in solid phase using one or combination of energy storage mechanisms including magnetic transformations, crystallographic structure transformations, order-disorder transformations, transformations between an amorphous structure and crystal structure. In general, the amount of latent heat of inorganic SS-PCMs is smaller compared to other types of solid-solid PCMs. Each single solid-solid transformation mechanisms exhibits a small amount of latent heat. Therefore, several solid-solid transformations should occur simultaneously to obtain large latent heats or heat storage/discharge at a specific temperature. There are a limited number of materials able to undergo multiple and reversible solid-solid transformations at close temperatures. Transformations between an amorphous structure and crystal structure are not reversible transformations as solid-solid transformations. ***Application:*** * One of the applications of inorganic SS-PCMs is in industrial plants for heat recovery of the intermittently emitted high-temperature waste heat. In this application, inorganic SS-PCMs utilizes one or two solid-solid transformations at high temperatures to store and later release of thermal energy in the solid phase.

4.1.1 Inorganic
The integration of solid-solid phase change material with micro-channel flat plate heat pipe-based BIPV/T
In this paper, the influence of the solid-solid phase change material on the novel micro-channel flat-plate heat-pipe–based building integrated photovoltaic/thermal system has been investigated, which has been expected to store the excess heat, enhance the overall efficiency of the system and maintain the stable photovoltaic temperatures. The proposed system was divided into two parts, i.e. the outdoor part formed by flat-plate glass, photovoltaic panel, micro-channel flat-plate heat pipes, solid-solid phase change material layer and insulated material, and indoor part including the storage tank, water pump and storage batter. The experiments were conducted at the Guangdong University of Technology, China, to investigate the thermal and electrical performance of the proposed system. When the simulated radiation was at 300 W/m2 and water flow rate was at 600 L/h, the maximum average thermal, electrical and overall efficiency were found at 52.9%, 7.9% and 60.8%, respectively, when the xenon lamps were turne...
11/01/2018 00:00:00
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4.1.2 Inorganic
Thermal energy storage: Recent developments and practical aspects
Abstract Thermal energy storage (TES) transfers heat to storage media during the charging period, and releases it at a later stage during the discharging step. It can be usefully applied in solar plants, or in industrial processes, such as metallurgical transformations. Sensible, latent and thermo-chemical media store heat in materials which change temperature, phase or chemical composition, respectively. Sensible heat storage is well-documented. Latent heat storage, using phase change materials (PCMs), mainly using liquid–solid transition to store latent heat, allows a more compact, efficient and therefore economical system to operate. Thermo-chemical heat storage (TCS) is still at an early stage of laboratory and pilot research despite its attractive application for long term energy storage. The present review will assess previous research, while also adding novel treatments of the subject. TES systems are of growing importance within the energy awareness: TES can reduce the LCOE (levelized cost of electricity) of renewable energy processes, with the temperature of the storage medium being the most important parameter. Sensible heat storage is well-documented in literature and applied at large scale, hence limited in the content of the present review paper. Latent heat storage using PCMs is dealt with, specifically towards high temperature applications, where inorganic substances offer a high potential. Finally, the use of energy storage through reversible chemical reactions (thermo-chemical storage, TCS) is assessed. Since PCM and TCS storage media need to be contained in a capsule (sphere, tube, sandwich plates) of appropriate materials, potential containment materials are examined. A heat transfer fluid (HTF) is required to convey the heat from capture, to storage and ultimate re-use. Particle suspensions offer a valid alternative to common HTF, and a preliminary assessment confirms the advantages of the upflow bubbling fluidized bed and demonstrates that particulate suspensions enable major savings in investment and operating costs. Novel treatments of the TES subject in the review involve the required encapsulation of the latent and chemical storage media, the novel development of powder circulation loops as heat transfer media, the conductivity enhancement of PCMs, the use of lithium salts, among others.
03/01/2016 00:00:00
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4.2 Organic

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Organic molecules capable of reorganizing their supramolecular interactions, typically hydrogen bonds, as a function of temperature, can potentially undergo highly endothermic solid-solid phase-transitions. These highly symmetric and bulky alcohols, such as aspentaerythritol (PE), neopentylglycol (NPG), trimethylolpropane(TMP), and pentaglycerine (PG) have been reviewed extensively. The pure compounds exhibit relatively high latent heats for their solid-solid phase transitions (above 100 J/g), at temperatures ranging from 40 °C to 190 °C. The transition temperatures can be tuned by producing eutectic mixtures of two of these compounds, in general lowering both the transition temperature and the phase change latent heat. Advantages * Freeze without much undercooling * Ability to melt congruently * Self nucleating properties * Compatibility with conventional material of construction * No segregation * Chemically stable * The high heat of fusion * Safe and non-reactive * Recyclable * Carbohydrate and lipid-based PCMs can be produced from renewable sources Disadvantages * Low thermal conductivity in their solid-state. High heat transfer rates are required during the freezing cycle. Nanocomposites were found to yield an effective thermal conductivity increase up to 216% * Volumetric latent heat storage capacity can be low * Flammable. This can be partially alleviated by specialist containment, or by incorporating environmentally friendly fire retardants ***Applications:*** * These compounds exhibit solid-solid phase change latent heats ranging from 102 J/g to 185 J/g, and transition temperatures ranging from 10 °C to 98 ° C.This behaviour makes them particularly attractive for a wide range of heat storage applications, and warrants follow up work to characterize the long term stability and cyclability.

4.2.1 Organic
Controlling heat release of crystallization from supercooling state of a solid-solid PCM, 2-amino-2-methyl-1,3-propanediol
Abstract The use of phase change materials (PCMs) for heat storage and as a heat source has become an important aspect for energy management. Some PCMs store energy when in a non-equilibrium state (a supercooling state), and supply energy when released from this state. This means PCMs have the ability to sustain heat energy for long periods and select the heat supply timing. 2-amino-2-methyl-1,3-propanediol (AMP), a solid-solid PCM, stores about 264 J/g of heat energy at the crystal transition temperature of about 78 °C. AMP has the attractive characteristic of storing heat energy in its solid supercooling state, similar to solid-liquid PCMs. In addition, AMP crystallizes from the supercooling state and releases heat energy of about 140 J/g during the heating process. These positive attributes make AMP a good candidate to assist in heating a system. This study applied this characteristic to methods handling the exoergic heat energy of the crystallization of AMP. First, the thermal properties are studied by DSC measurement and thermal cycle tests in different mass conditions. Second, the crystallization is investigated by observation of crystal growth. The results show that the supercooling state crystallizes with exoergic heat during the heating process. It turns out that the crystal nucleation rate (1/s) highly depends on the temperature and AMP mass. The crystal growth rate (μm/s) is acquired in this experiment. By using this information, it is possible to handle the exoergic heat of the crystallization from the supercooling state by changing the AMP mass and minimum temperature during cooling. Moreover, the heat energy that is kept in the supercooling state can be also controlled by crystal nucleus addition or impact.
07/01/2019 00:00:00
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4.2.2 Organic
The integration of solid-solid phase change material with micro-channel flat plate heat pipe-based BIPV/T
In this paper, the influence of the solid-solid phase change material on the novel micro-channel flat-plate heat-pipe–based building integrated photovoltaic/thermal system has been investigated, which has been expected to store the excess heat, enhance the overall efficiency of the system and maintain the stable photovoltaic temperatures. The proposed system was divided into two parts, i.e. the outdoor part formed by flat-plate glass, photovoltaic panel, micro-channel flat-plate heat pipes, solid-solid phase change material layer and insulated material, and indoor part including the storage tank, water pump and storage batter. The experiments were conducted at the Guangdong University of Technology, China, to investigate the thermal and electrical performance of the proposed system. When the simulated radiation was at 300 W/m2 and water flow rate was at 600 L/h, the maximum average thermal, electrical and overall efficiency were found at 52.9%, 7.9% and 60.8%, respectively, when the xenon lamps were turne...
11/01/2018 00:00:00
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4.3 Organo-Metallic

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Organometallic SS-PCM is a group of layer perovskite organometallics, which are composed of alternate inorganic and organic layers and have a sandwich-like crystalline structure. The pure compounds exhibit relatively high latent heats for their solid-solid phase transitions (above 100 J/g), at temperatures ranging from 40°C to 190°C. The transition temperatures can be tuned by producing eutectic mixtures of two of these compounds, in general lowering both the transition temperature and the phase-change latent heats. Organometallic SS-PCM can be described with the general chemical formula (n-CnH2n+1NH₃)2MX₄ , where M is a metal atom, X is a halogen, and n varies from 8 to 18. The organic region consists of long paraffinic chains of n-alkylammonium groups, which are attached to the thin inorganic layer through ionic bonds. ***Applications:*** * the thermal conductivity of organometallic SS-PCMs is higher than n-paraffin by an order of magnitude because of high thermal conductivity of the metals in the inorganic region, although no experimental results have been reported in the literature yet. However, the relatively high densities of organometallic SS-PCMs make them less suitable for weight-sensitive applications.

4.3.1 Organo-Metallic
Properties and reactivity of LaCuxNi1−xO3 perovskites in chemical-looping combustion for mid-temperature solar-thermal energy storage
Abstract Solar-heat driven chemical-looping combustion (S-CLC) is an efficient method for storing solar energy. In the S-CLC process, solar heat is used to drive the endothermic reduction reaction between a hydrocarbon fuel and an oxygen carrier. The solar heat is converted into chemical energy and stored in the reduced oxygen carrier. Owing to their high reactivity at low reaction temperatures, perovskites are treated as promising oxygen carriers in S-CLC. Herein, the reactivity and regenerability of LaCu x Ni 1−x O 3 (x = 0.025, 0.050, 0.075, 0.1, 0.2, 0.3, 0.5) perovskites are studied using methane as the fuel gas. The experimental results show that LaCu 0.1 Ni 0.9 O 3 has the highest reactivity and regenerability among the synthesized materials. At a reduction temperature of 350 °C, more than 46% of the LaCu 0.1 Ni 0.9 O 3 is reduced in 5 min, much higher than the amount of other LaCu x Ni 1−x O 3 perovskites reduced under the same conditions. After 30 redox cycles, the reactivity and micrographs of LaCu x Ni 1−x O 3 are similar to those of fresh material, indicating that LaCu 0.1 Ni 0.9 O 3 has a desirable regenerability. Furthermore, no carbon deposition is observed during the reduction reaction between CH 4 and LaCu x Ni 1−x O 3 . Our study is expected to provide a new method for storing mid-and-low temperature solar heat using this solid perovskite.
10/01/2018 00:00:00
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4.4 Polymeric

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Attachment or incorporation of a phase changing motif into a polymeric structure will be accompanied by a decrease in the observed latent heat. This reduction on the energy absorbed during the phase transition is due to several factors: (a) dilution of the phase changing moieties within a thermally inert polymeric matrix, (b) mobility or packing restrictions of the crystallizing groups due to attachment, (c) strong interaction of the phase changing moieties with the polymer backbone. The magnitude of the decrease in the observed latent heats depends on the choice of the polymer backbone and phase changing motifs. Also more information available [here](https://reader.elsevier.com/reader/sd/pii/S1359431117329939?token=F3E55D40A856580F2188E89A722387D50B5EA5DF9D550BFDE7F622789008B95FE03FE254E5D8DF93A9010EE6953547D0). ***Applications:*** * From a materials design perspective, the use of polymeric structures as a form stabilizing matrix and as mechanical support is definitively attractive. However, the observed decreases in the resulting phase change latent heats, compared to those for the untethered phase-changing moiety suggest that direct covalent attachment of the phase changing motif to the polymeric backbone may not be the best course of action. * Polymeric SS-PCMs show many similarities to various smart polymer systems, many of whom also employ phase transitions, for example, to bring about changes in hydrophobicity or transparency. New multifunctional SS-PCMs can be developed that combine thermal energy storage with other useful functional attributes. Such integrated and multifunctional approaches can lead to the development of innovative adaptive materials that can self-regulate their heat storage and thermal transport properties in response to various external stimuli. Examples abound in biological systems were optical, thermal, and structural functions render adaptive systems enabled by various phase transformations ( More information available [here](https://www.sciencedirect.com/science/article/pii/S1359431117329939). * A recent study investigated an adaptive passive solar building enclosure system using a thin layer of polymeric SS-PCM, which was used as a coating onto a highly reflective exterior façade material. * Semiconductors in PC modules, LED Chip-onboard modules (see Shi-Etsu).

4.4.1 Polymeric
A novel form-stable phase change composite with excellent thermal and electrical conductivities
Abstract Electro-to-heat energy conversion/storage provides a new direction for the development of phase change materials (PCMs). However, conversion rate and energy storage density of the existing PCMs are limited by their low intrinsic electrical and thermal conductivities and poor compressive strength. In this work, a novel form-stable phase change material (FSPCM) has been prepared via ligand replacement followed by the embedment of acetylene black conductive network. The addition of 20 wt% acetylene black reduces the resistivity of the polyethylene glycol-based PCM from 10 7 −10 12  Ω·m to 0.3 Ω·m, while its thermal conductivity is increased by 300%. The resulting conductive composite possesses the ability to store heat at voltage as low as 1.8 V and high electro-to-heat conversion efficiency. The composite compressive strength reaches 10 5 Pa at an ambient temperature of 110 °C, while the temperature is 60 °C more than that of phase transition temperature of PCM. Further, the magnitude of the temperature change in the electrothermal conversion curves recorded after 50 solid-liquid phase transition cycles does not exceed 2.0%. The excellent electrical and thermal conductivities as well as good mechanical properties of the synthesized composite suggest a promising route for manufacturing novel materials with high power capacity for thermal storage applications.
03/01/2018 00:00:00
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4.4.2 Polymeric
Polymer-stearic acid blends as form-stable phase change material for thermal energy storage
Received 04 March 2005; revised 05 September 2005; accepted 07 October 2005 This paper determines thermal properties of blends of polyvinyl alcohol (PVA)-stearic acid (SA) and polyvinyl chloride (PVC)-stearic acid (SA) as form-stable phase change material (PCM) for thermal energy storage (TES). In the blends, SA has a function of storing latent heat of fusion during its solid-liquid phase change when the polymer (PVC or PVA) as a supporting material prevents melted SA leakage because of its structural strength. Therefore, such blend is formstable and can be used as PCM without encapsulation for passive solar TES applications. The maximum amount of SA in both composites found as high as 50 wt% without any seepage of SA in melted state. The dispersion of SA into the network of solid polymer matrix was investigated using an optical microscope (OM). The miscibility of SA with PVA and PVC were proved by Fourier Transfer Infrared (FT-IR) Spectroscopy method. Furthermore, melting temperatures of SA in PVA-SA and PVC-SA blends with form-stable mass combination (50 wt% polymer-50 wt% SA) and the total latent heats of fusion of the blends were found as 67.4 °C and 64.7 °C, and 132.68 and 129.34 J/g, respectively by Differential Scanning Calorimetry (DSC). Polymer-stearic acid blends as form-stable composite PCM were found to have great potential for especially solar space and building heating applications in terms of their satisfactory thermal properties and cost-effectivity.
12/01/2005 00:00:00
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5. Solid-liquid latent heat storage (SL-LHS)

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Generally, LHS systems use the latent heat between solid and liquid phases of the storage medium, whereby the PCM is required to be contained or encapsulated within a container to prevent the liquid from leaking; however, the capsules decrease the energy density of the system and increase the cost of production. Such storage has potential in heating and cooling buildings, waste heat recovery, offpeak power utilization, heat pump systems, tanks and many other applications. In general PCM materials have specific energy within the range of 50-150 kWh/t with an energy capacity of 100 kWh/m³. The efficiency of these systems is around 75-90% and storage periods are mostly hour-week based. The power which can be retrieved from these system is around 0.001-1 MW depending on the size. The cost of the PCM is around 10-50 €/kWh.


5.1 Non-paraffins (Organic)

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The non-paraffin organic (fatty acids, esters, and alcohols) are the most numerous of the phase change materials with highly varied properties. They are highly flammable and therefore, should not be exposed to intense temperature, flames or oxidizing agents. Non-paraffin organic materials are further subgroups as fatty acids and other non-paraffin organic materials. Among the non-paraffin organic PCMs, fatty acids are relatively cheaper, although their cost remains 2–2.5 times higher than technical grade paraffin's. Some commercial organic PCMs are shown in the figure with their properties. The organic non-paraffin group usually has a melting point around 8-187 °C with a heat of fusion of 130-250 J/kg K. Advantages of organic fatty acids and organic paraffin's: * Crystallize with no or little supercooling * Ability to melt congruently * Self-nucleating properties * Thermally stable for repeated cycles * Compatibility with conventional material of construction * No segregation * Chemically stable * High heat of fusion * Safe and non-reactive * Recyclable * Small volume change Disadvantages of organic fatty acids and organic paraffin's: * Low thermal conductivity in their solid-state (\~0.2 W/m K) * Low volumetric latent heat storage capacity * Flammable * High costs * Non-compatible with plastic containers ***Applications:*** * not often used for electronics heat sink * Solar heating systems * Temperature-controlled packaging

5.1.1 Non-paraffins (Organic)
Embodied energy in thermal energy storage (TES) systems for high temperature applications
Currently, there is an increasing interest in concentrated solar power (CSP) plants as alternative to produce renewable electricity at large scale by using mirrors to concentrate the solar energy and to convert it into high temperature heat. These facilities can be combined with thermal energy storage (TES) systems, which are, nowadays, one of the most feasible solutions in facing the challenge of the intermittent energy supply and demand. However, they are still in research process and, for that, there is a lack of environmental impact studies of these TES systems complementing solar plants. This paper accounts the environmental impact of three TES systems used nowadays in high temperature applications for CSP plants: first, a system which stores sensible heat in high temperature concrete; second, a system storing sensible heat in molten salts; and third, another system with molten salts but storing latent heat. All the systems are normalised in order to be comparable between them due to its initial storage capacity difference. The environmental impact is accounted by calculating the amount of embodied energy in the components of the different TES systems. Notice that embodied energy refers to the total energy inputs required to make a component. Between the three systems, the sensible heat system using concrete as storage material is the one with less environmental impact while the molten salts and PCM have a higher value of embodied energy, mainly due to the nitrate mixture used as storage material. Finally, advantages and disadvantages of the method proposed used are discussed.
01/01/2015 00:00:00
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5.1.2 Non-paraffins (Organic)
Experimental Investigation on a Solar Thermal Energy Packed Bed Sensible Heat Storage Combined with Latent Heat Storage
The thermal energy storage is required to store the solar energy, which can be stored by using sensible, latent and thermo-chemical heat storage energy systems. The sensible heat storage is more reliable and full-fledged technology, but it is low efficient due to low heat storage density. In the present study, experimental setup is developed by combining the sensible heat storage with a latent heat storage unit in order to store the solar energy. The developed thermal energy storage unit contains an insulated cylindrical tank having hollow spherical capsules of HDPE (filled with fatty acid which has phase-change property). The water and oil liquid transport medium is used as a heat-carrying substance which works as a transporting heat energy from high-temperature container to TES tank and act as SHS materials. The temperature of the transport medium is maintained constant at inlet of the tank during charging and discharging processes. The effect of flow rate and inlet temperature of HTF is analyzed on charging time with the help of charging experiments. The performance parameters viz. cumulative heat stored and efficiency are analyzed during charging and discharging processes. The result shows that efficiency of the system with water as HTF is more than that of oil.
01/01/2019 00:00:00
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5.1.3 Non-paraffins (Organic)
Heat capacities of potential organic phase change materials
Abstract The heat capacity of a material is an important factor for many applications, including phase change material (PCM) selection for thermal energy storage. Aside from storing energy via the latent heat of a phase transition, significant sensible heat can be stored using the material’s heat capacity outside the transition temperature region. Furthermore, accurate heat capacity values are required to model and thereby optimize PCM heat storage systems. Various group additivity models can be used to estimate the heat capacity of organic liquids. However, these methods do not distinguish isomers built of the same base units. In the present study the liquid phase heat capacities of five isomeric, 12-carbon, linear, saturated fatty esters (potential PCMs) have been measured experimentally, and the results are compared to calculations from several group additivity methods. It was found that the heat capacities of the liquid esters are well described by the group additivity models, and that each of the esters had approximately the same heat capacity at a given temperature, despite their structural differences. The heat capacity of another isomer, dodecanoic acid, was also compared to the ester isomers, and found to be significantly different. The group additivity methods also were able to accurately represent the heat capacity of the acid isomer.
01/01/2019 00:00:00
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5.1.4 Non-paraffins (Organic)
High temperature latent heat thermal energy storage: Phase change materials, design considerations and performance enhancement techniques
A very common problem in solar power generation plants and various other industrial processes is the existing gap between the period of thermal energy availability and its period of usage. This situation creates the need for an effective method by which excess heat can be stored for later use. Latent heat thermal energy storage is one of the most efficient ways of storing thermal energy through which the disparity between energy production or availability and consumption can be corrected, thus avoiding wastage and increasing the process efficiency.
11/01/2013 00:00:00
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5.1.5 Non-paraffins (Organic)
Integration highly concentrated photovoltaic module exhaust heat recovery system with adsorption air-conditioning module via phase change materials
Highly concentrated photovoltaic (HCPV) module exhaust heat recycle system incorporated with adsorption air-conditioning (AAC) module and PCM, along with providing domestic hot water was designed and discussed. In light of the different grade of thermal energy, several operating modes were analyzed in this system. Besides, an appropriate composite phase change material (CPCM) was obtained to store the waste heat of HCPV module. Acetamide (AC)/expanded graphite (EG) composite phase change material (CPCM) was obtained. The phase change temperature and latent heat of AC/EG CPCM were 71.50 °C and 162.2 J g−1, respectively, which was characterized by differential scanning calorimeter (DSC). Thermal cycling test of the CPCM performed good thermal reliability with minor variation in thermal properties after 300 thermal cycling. The thermal conductivity of AC/EG CPCM was 6.159 W m−1 K−1, close to 15.83 times of pure AC. The enhancement of thermal conductivity of AC/EG CPCM can also be confirmed by the less thermal response to storage/release latent heat time. Furthermore, an effective theoretical model was proposed to predict the thermal conductivity of AC/EG CPCM blocks with various packing densities. Consequently, the obtained AC/EG CPCM can be a promising material to integrate HCPV module exhaust heat recovery system with AAC module, and offering domestic hot water simultaneously.
01/01/2017 00:00:00
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5.1.6 Non-paraffins (Organic)
PCM-Graphite Latent Heat Storage Systems for Industrial Process Heat Recovery
Increasing energy prices and shortage of fossil fuels lead to a growing interest in alternative energy sources. In combination with energy storage systems the generation of solar process heat can be provided independent from the weather leading for example to a cost efficient stabilization of power output. For this application latent heat storage units with phase change materials (PCMs) can be designed to store solar process heat within a narrow temperature interval utilizing the high storage density of the different PCMs. This is achieved using the latent heat of melting in the melting / solidification process, or the latent heat of re-crystallization in a solid / solid phase transition. However, this advantage can only be used in technical applications if the heat transfer in the PCM is sufficiently high. As most pure PCMs exhibit a low thermal conductivity (about 1 W/(m•K) or less), methods to improve heat transfer in PCMs have been under investigation for decades. The heat transfer in a PCM can be increased by addition of highly thermal conductive materials. Due to its superior properties - high thermal conductivity, good processability, and chemical inertness - graphite has distinct advantages for this purpose. Depending on the requirements of the respective application, various routes to combine PCM and graphite are used. For example, besides the fabrication of PCM/graphite composite materials, the increase of heat exchanger surface by highly thermal conductive graphite plates is a favorable method for large scale applications, in particular. Effective thermal conductivities up to 30 W/(m•K) have been realized. This paper gives an overview of actual and potential applications of PCM/graphite heat storage systems focusing on storage of solar heat for high temperature applications such as process heat generation and solar thermal power plants.
10/01/2010 00:00:00
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5.1.7 Non-paraffins (Organic)
Thermal conductivity enhancement of recycled high density polyethylene as a storage media for latent heat thermal energy storage
Abstract In the context of reducing CO 2 emissions and balancing energy supply and demand across the electricity grid, energy storage has become an important topic. Therefore, new energy policies are looking for more efficient and environmental friendly technologies. The aim of this research is to assist in the implementation of the renewable energies technologies and to improve the energy efficiency in well-known and established processes by recovering and storing heat. Moreover, the use of a recycled material as a storage media for thermal energy storage applications shows a more sustainable use of resources reducing at the same time the overall cost. In this research a novel composite, a recycled high density polyethylene (HDPE)/graphite(Cg) mixture, for medium temperature thermal energy storage application has been formulated and characterized. One common characteristic of polymers is their low thermal conductivities. This causes a slow thermal response when the PCM is used in high power applications. In this study the thermal conductivity properties of the HDPE/Cg were enhanced by the optimization of its manufacturing process and composition. Graphite content was added in different mass fractions into the PCM, and thermal properties were measured by means of Thermogravimetric analysis (TGA), Differential scanning calorimetry (DSC) and Laser Flash Analysis (LFA). The experimental results showed that the thermal conductivities are improved by the higher mass fraction of graphite. When the graphite content was in the ratio of 20 wt%, the thermal conductivity of the PCM increased from 0.51 W m −1  K −1 up to 1.31 W m −1  K −1 . The secondary electron microscopy confirms a good homogeneity of the manufacturing process. Further chemical stability analysis was performed by means of charging and discharging processes. The cycled samples present good thermal property reliability at temperatures up to 250 °C.
08/01/2016 00:00:00
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5.2 Paraffin (Organic)

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Paraffin is non-corrosive, chemically inert and stable below 500 °C, show little volume changes on melting and have low vapour pressure in the melt form, therefore are one of the more utilized PCM, Paraffin is a petroleum derivative organic material (an alkane hydrocarbon with long straight n-alkane chains as the composition of “CH₃− (CH₂)n – CH₃”) chemically inert and stable below 500 °C. They have many other characteristics such as repeated melting and freezing without phase segregation and consequent degradation of their latent heat of fusion, low vapour pressure during melting, crystallize with little or no supercooling condition, noncorrosive, chemically stable, low cost and largely available. However, they present low thermal conductivity, are non-compatible with the plastic container and flammable. These adverse properties can be improved and solved by encapsulating the paraffin in a suitable container. Parrafin, in general, have a melting temperature of -5-120 °C with a melting enthalpy in the range of 150-240 kJ/kg and a density of 0.77 g/cm³. Some commercial paraffin structures are shown in the figure. ***Applications:*** * Paraffin is the most common PCM for electronics thermal management. They are chemically compatible with most metals. They have large latent heat and can be obtained over a wide temperature range. * Datacenters * Clothing * Packaging

5.2.1 Paraffin (Organic)
Characterization of Alkanes and Paraffin Waxes for Application as Phase Change Energy Storage Medium
Abstract Latent thermal energy storage is one of the favorable kinds of thermal energy storage methods considered for renewable energy source utilization, as in solar photothermal systems. Heat is stored mostly by means of the latent heat of phase change of the medium. The temperature of the medium remains more or less constant during the phase transition. A large number of materials have been identified for low, intermediate, and high operating temperatures for application as latent thermal energy storage media. In the present paper a method for characterization of alkanes (C1,-C100) and paraffin waxes for application as the low-temperature (298-323 K) phase change energy storage medium is introduced. A computational technique is introduced by which the alkanes and paraffin waxes could be evaluated, and possibly upgraded, as the phase change energy storage media. It is demonstrated that the family of n-alkanes has a large spectrum of latent heats, melting points, densities, and specific heats so that the...
01/01/1994 00:00:00
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5.2.2 Paraffin (Organic)
Experimental investigation of latent heat storage in a coil in PCM storage unit
Abstract The thermal energy storage is very important because it provides the solution to problems related between the provided and the required energies. This work presents the experimental study of a PCM storage unit for storing latent heat thermal energy. Three different types of paraffin are tested as phase change material (PCM) and water is used as heat transfer fluid (HTF). The temperatures of PCM and HTF, solid fraction and thermal effectiveness are analyzed. The effects of inlet temperature of HTF, flow rate of HTF and the type of PCM used on the time for charging and discharging heat are discussed. The following conclusion can be drawn: (1) HTF flow rate does not have a great effect on the discharging phase compared to the charging phase. (2) Inlet temperature has a great effect on the exchanger performance. It can accelerate charging phase 54.5% and delay the discharging phase by 48.5%. (3) Adding the oil engine to the paraffin can improve the speed of the charging and discharging heat process by 42.4 and 66%, respectively. However, the latent heat of the PCM is considerably reduced.
02/01/2016 00:00:00
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5.2.3 Paraffin (Organic)
Experimental Studies on Performance of Latent Heat Thermal Energy Storage Unit Integrated with Solar Water Heater
The energy storage leads to saving premium fuels and makes the system more cost effective by reducing the wastage of energy. Solar is being a renewable energy, which is used to store heat in the storage tank and PCM encapsulated copper tubes are kept inside the storage tank called PCM storage tank. Thealmost 90 copper tubes is used and phase change materials are filled in each tube. The varieties of PCM materials are analyzed, and suitable material is to be selected for thermal storage system. Copper tube encapsulated with paraffin wax (PCM) is going to be designed and fabricated to store the heat energy in PCM storage tank. Large quantity of solar thermal energy is absorbed in the day time. During charging process heat can be stored in copper tube as latent heat, the same heat can be stored during discharging process by applying cold water. The PCM used is intended to enhance the heat storage capacity of the conventional solar tanks used in domestic solar heaters and to measure inlet and outlet water temperature. The tank is continuously monitored and various sets of readings are recorded at regular time intervals and graphs are to be plotted. The temperature distribution in HTF and PCM’s are going to be analysed by using computational fluid dynamics at steady state and transient conditions.
01/01/2016 00:00:00
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5.2.4 Paraffin (Organic)
Heat transfer characteristics of high melting point paraffin emulsions for latent heat transportation
The latent heat transportation materials with high melting points,paraffin emulsions,can be used as heat storage and transfer media.Because paraffin emulsions can store their latent heat during phase change process in the temperature range of 80—90℃,their heat storage density is higher than water.They can be applied for waste heat recovery,solar energy utilization or central heating systems.In the forced convection heat transfer experiments,the thermal boundary conditions of constant heat flux were imposed.Although the paraffin emulsions have higher effective specific heat capacity,the convective heat transfer coefficients are lower than that of water and decrease with the increase of concentration.The results also show that the convection heat transfer coefficient increases with temperature slightly.The correlations of Nusselt number for paraffin emulsions are obtained according to the experimental data.
01/01/2012 00:00:00
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5.2.5 Paraffin (Organic)
High temperature latent heat thermal energy storage: Phase change materials, design considerations and performance enhancement techniques
A very common problem in solar power generation plants and various other industrial processes is the existing gap between the period of thermal energy availability and its period of usage. This situation creates the need for an effective method by which excess heat can be stored for later use. Latent heat thermal energy storage is one of the most efficient ways of storing thermal energy through which the disparity between energy production or availability and consumption can be corrected, thus avoiding wastage and increasing the process efficiency.
11/01/2013 00:00:00
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5.2.6 Paraffin (Organic)
Low temperature paraffin phase change emulsions
Abstract A paraffin phase change emulsion is a multifunctional fluid consisting of water as the continuous phase and a paraffin as the dispersed phase. It can store or transfer large amounts of thermal energy by using the latent heat capacity of the paraffin during the solid–liquid transition as well as the sensible heat capacity of water and that of the paraffin. This paper presents three paraffin emulsions with different phase transition temperatures: CryoSol plus 6, CryoSol plus 10 and CryoSol plus 20. CryoSol plus 6 is foreseen for air-conditioning applications with a freezing peak point of 6 °C, CryoSol plus 10 for cooling of buildings with a freezing peak point of 10 °C and CryoSol plus 20 for increasing the thermal storage mass of building components with a freezing peak point of 20 °C.
12/01/2010 00:00:00
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5.2.7 Paraffin (Organic)
Performance of Latent Heat Solar Thermal Energy Storage System Using Various Heat Transfer Fluids
In the present work the thermal performance of Phase Change Material (PCM) based solar thermal energy storage system under the influence of different heat transfer fluids (HTF) have been investigated. Water, Ethylene Glycol–water and Copper nanofluid are selected as HTF. Paraffin is used as PCM and encapsulated in cylindrical capsules. The thermal energy storage (TES) tank acts as a storage unit consisting PCM capsules packed in three beds surrounded by water, which acts as sensible heat storage (SHS) material. HTF circulated by a pump transfers heat from solar flat plate collector (FPC) to the TES tank. 25% ethylene glycol -75% water HTF is prepared by mixing ethylene glycol (EG) with water. Copper-distilled water nanofluids (0.3% by weight) are prepared using prolonged sonication with sodium dodecyl benzene sulphonate (SDBS) as the surfactant. Various performance parameters such as charging time, instantaneous heat stored, cumulative heat stored and system efficiency are studied for various HTFs. It is found that the charging time is reduced by 33.3% for copper nanofluid and 22.2% for ethylene glycol- water mixture HTFs. It is also observed that there is an increase in system efficiency and cumulative heat stored with reference to charging time for these HTFs when compared with conventional HTF 1 i.e. water.
08/01/2015 00:00:00
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5.3 Metallic alloys (Inorganic)

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Constraints, due to high volumetric fusion heat, they are a good candidate. The use of metal/metallic materials poses a number of engineering problems during design, development and exploitation of the storage system.\ A new concept of MgH₂ tank was developed to store the heat of reaction by using phase-change material (PCM). The heat of desorption is mainly provided by the latent heat of solidification of the PCM. Ex: A metallic alloy based on Mg–Zn eutectic was selected as PCM in order to enhance the thermal exchange with the MgH₂ compacts. ***Applications:*** * Metallic PCMs are generally used at high temperatures, where no suitable paraffin wax is available.

5.3.1 Metallic alloys (Inorganic)
A new MgH2 tank concept using a phase-change material to store the heat of reaction
The formation of magnesium hydride under hydrogen pressure is highly exothermic. The enthalpy of reaction represents 31% of the lower heating value (LHV) of the absorbed hydrogen. A new concept of MgH2 tank was developed to store the heat of reaction by using a phase-change material (PCM). The heat of desorption is mainly provided by the latent heat of solidification of the PCM. A metallic alloy based on Mg-Zn eutectic was selected as PCM in order to enhance the thermal exchange with the MgH2 compacts. A pilot tank of about 7000 NL of hydrogen was designed and tested under various experimental conditions. Desorption was achieved in 3 h and the daily storage efficiency was around 70%.
08/01/2013 00:00:00
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5.3.2 Metallic alloys (Inorganic)
An experimental study on the corrosion sensitivity of metal alloys for usage in PCM thermal energy storages
Abstract The vast majority of renewable energy systems, especially solar ones, include thermal energy storage (TES). TES with phase change materials (PCMs) are now an established technology in several applications, but their commercialization and mass introduction cannot ignore reliability, in terms of service life of components. Among PCMs, salt hydrates are widely used but are potentially corrosive. In the present paper, the corrosion behaviour of three metal alloys (AISI 1050 carbon steel, AA 6061 aluminium and CW024A copper alloys) is investigated with magnesium nitrate hexahydrate molten salt at 120 °C. Contrary to previous studies, the study is not based on visual observation or mass loss, but corrosion sensitivity is instead studied via electrochemical impedance spectroscopy (EIS). The results highlight that good corrosion stability was observed for the aluminium alloy, since no evidence of corrosion phenomena were observed on its surface. However, carbon steel and copper alloys show significant electrochemical activity, together with a large amount of corrosion products, after just a few hours of immersion in the severe environmental conditions. Corrosion mechanisms were proposed by fitting EIS curves with several equivalent circuits, therefore suggesting design approaches for PCM-TES systems.
08/01/2019 00:00:00
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5.3.3 Metallic alloys (Inorganic)
Effect of domain subdivisions on alloy solidification
Abstract The sensible heat portion of thermal energy storage (TES) for concentrated solar power (CSP) can be achieved using off-eutectic materials. These materials have the advantage of storing in latent as well as sensible heat through a given temperature range. On the other hand, off-eutectic materials have the disadvantage of possibly experiencing segregation effects, most likely impairing their solidification. During solidification, macrosegregation can occur due to a number of possible causes such as density differences in the solid and liquid portions of the mixture/alloy, flows due to capillary forces, flows due to electromagnetic fields or forced stirring, etc. In some cases, macrosegregation can severely affect solidification. One possible means to limit this segregation is with porous media. In this study, the segregation of an off-eutectic material in a porous medium is studied. Pore sizes and porous medium thermal conductivity are varied, revealing the importance of various mechanisms affecting solidification. Smaller pore sizes and higher porous medium thermal conductivities are shown to improve segregation and solidification.
06/01/2018 00:00:00
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5.3.4 Metallic alloys (Inorganic)
High temperature latent heat thermal energy storage: Phase change materials, design considerations and performance enhancement techniques
A very common problem in solar power generation plants and various other industrial processes is the existing gap between the period of thermal energy availability and its period of usage. This situation creates the need for an effective method by which excess heat can be stored for later use. Latent heat thermal energy storage is one of the most efficient ways of storing thermal energy through which the disparity between energy production or availability and consumption can be corrected, thus avoiding wastage and increasing the process efficiency.
11/01/2013 00:00:00
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5.3.5 Metallic alloys (Inorganic)
Investigation of In–48Sn as a phase change material candidate for thermal storage applications
Latent heat storage systems provide large thermal storage densities for solar energy storage for various domestic and industrial applications. In–48Sn, an alloy of indium and tin a lead-free solder is investigated as a phase change material (PCM) in latent heat storage systems for heating applications. Results obtained from differential scanning calorimetry indicate that the alloy is useful in storing sensible heat beyond its melting temperature as it exhibits very little decomposition up to 400 °C. Though In–48Sn possesses a low latent heat of fusion, its high density allows for a larger thermal storage mass. The behaviour of In–48Sn in a 50 mm aluminium spherical capsule during charging and discharging cycles is investigated using sunflower oil as the heat transfer fluid (HTF) at flow rates of 3, 6, 9 and 12 ml/s. The influence of the charging temperature on the charging characteristics of the encapsulated PCM is also investigated. The average charging and discharging rates of the encapsulated PCM show an increase with an increase in the HTF flow rate. The HTF temperature determines the maximum temperature attained by the PCM and thus the total energy stored by the encapsulated PCM. In–48Sn shows good potential as a PCM in a spherical aluminium capsule for packed bed domestic heat storage systems.
01/01/2017 00:00:00
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5.4 Salt Hydrates and compositions (Inorganic)

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The solid-liquid transformation of salt hydrates is actually dehydration of salt that resembles melting or freezing thermodynamically. Salt hydrates can be considered as alloys of inorganic salts (AB) and water (H₂O), resulting in a typical crystalline solid with the general formula (AB x H₂O). A salt hydrates usually melt to either to a salt hydrate with fewer moles of water or to its anhydrous form. During the charging phase, the thermal energy is stored by performing the dehydration reaction of a hydrated salt. During the discharging phase, the stored heat is released by undergoing the hydration reaction of the salt. This process is achieved by the addition of water vapour to anhydrous salt. In general, inorganic compounds have near twice the energy storage capacity per volume unit than organic compounds and they possess much higher operating temperatures. Salts have been extensively studied for their use in LHTES systems. They present a high latent heat of fusion per unit volume, a higher thermal conductivity than paraffin׳s and small volume changes on melting also compatible with plastics, non-flammables, but are slightly toxic, present supercooling and nucleation problems and corrosive to most metals. The high heat of fusion of chlorides and fluorides and the low cost of the former have encouraged further studies of salt compositions on their basis. Advantages of inorganic salt hydrates: * High volumetric latent heat storage capacity * Availability and relatively low cost * Sharp melting point * High thermal conductivity * Non-flammable Disadvantages of inorganic salt hydrates: * Change of volume is very high * Supercooling is a major problem in the solid-liquid transition * Nucleation agents are needed, and they often become inoperative after repeated cycling ***Applications:*** * These are not commonly used for electronics heat sinks since they are corrosive and long term reliability (thousands of cycles) is uncertain. * The most common application is for very large thermal storage applications (e.g., solar heating), where much lower cost is very attractive. * Used for air conditioning * This range of PCMs can be used in a number of applications, primarily involving heat storage or thermal shielding. Their high densities and high latent heat values make them particularly effective PCMs. * Grid balance (SaltX)

5.4.1 Salt Hydrates and compositions (Inorganic)
Carbonate salt based composite phase change materials for medium and high temperature thermal energy storage: A microstructural study
Abstract We investigated the microstructures and their formation mechanisms of carbonate salt based composite phase change materials (CPCMs). Such materials typically consist of a carbonate salt as the phase change material (PCM), a thermal conductivity enhancement material (TCEM) and a ceramic skeleton material (CSM) for structure stabilisation, and are mainly for medium and high temperature thermal energy storage applications. Two carbonate salt based composites were studied with one being eutectic NaLiCO 3 and the other Na 2 CO 3 . MgO and graphite flakes were used respectively as the CSM and TCEM for fabricating the composite modules. A scanning electron microscope with energy dispersive spectrometer (SEM-EDS) was used to observe the microstructures and the salt distribution and redistribution within the composite structures during repeated melting-solidification cycles. The results showed salt migration within the composite structure during the thermal cycling. Such a microscopic motion led to a more homogenous distribution of not only the salt but also the CSM and TCEM. At a low graphite flake loading, breakage of the graphite flake was observed, suggesting stress generation during thermal cycling. The extent of the breakage reduced with increasing graphite flake loading, suggesting the stress generation be related to microscopic motion. The MgO based CSM particles were likely to be sintered, forming a porous structure. Such a structure reduced the swelling effect partially due to the use of graphite on which the salts had a poor wettability.
07/01/2019 00:00:00
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5.4.2 Salt Hydrates and compositions (Inorganic)
High temperature latent heat thermal energy storage: Phase change materials, design considerations and performance enhancement techniques
A very common problem in solar power generation plants and various other industrial processes is the existing gap between the period of thermal energy availability and its period of usage. This situation creates the need for an effective method by which excess heat can be stored for later use. Latent heat thermal energy storage is one of the most efficient ways of storing thermal energy through which the disparity between energy production or availability and consumption can be corrected, thus avoiding wastage and increasing the process efficiency.
11/01/2013 00:00:00
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5.4.3 Salt Hydrates and compositions (Inorganic)
Properties of some salt hydrates for latent heat storage
For the utilization of low-grade heat the latent storage of thermal energy is of great advantage because the heat can be preserved at a constant temperature perfectly matched to the special purpose of application. Investigations on the heat capacities, enthalpies of fusion, densities, crystallization behaviour and other chemical and physical properties have shown that the following salt hydrates are especially suitable media for storing low-grade heat. The eutectic mixture of water and 3.92% by weight of sodium fluoride, melting point (MP) = - 3.5°C, is extremely convenient and cheap for refrigerating or other cooling purposes. Lithium chlorate trihydrate, LiClO3. 3H2O, MP = +8.1°C has an extremely high storage capacity and other advantageous properties as a storage medium in cooling systems, but a very high price will limit its application. Calcium chloride hexahydrate, CaCl2. 6H2O, MP = + 29.2°C, is a suitable and cheap storage medium for heating purposes. For the same application disodium hydrogen phosphate dodecahydrate, Na2HPO4. 12H2O, MP = + 35.2°C, is even better because of the larger storage capacity per unit volume and other advantages which largely compensate the higher material cost. the unique properties of potassium fluoride tetrahydrate, KF. 4H2O, MP = +18.5°C, make it especially suitable for storing low-grade heat. It can directly function as an energy sink and as an energy reservoir in heat collecting and consuming systems. Examples of the practical applicability for residential heating, temperature levelling and cooling are described.
01/01/1977 00:00:00
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5.4.4 Salt Hydrates and compositions (Inorganic)
R and D of Systems for Thermal Energy Storage in the Temperature Range from -25°C to 150°C
The investigations of materials presumably suitable as storage media for latent heat indicate that water, some salt hydrates and eutectic mixtures of water and salt hydrates possess extreme heats of fusion. Their melting points, ranging from about -50° to +130°C, fit well for storing low grade heat in residential energy systems. Detailed experimental investigations on a large number of these media show, however, that only a few of them suffice the quality requirements for practical application in storage units.
01/01/1980 00:00:00
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5.4.5 Salt Hydrates and compositions (Inorganic)
Thermal conductivity enhancement of hydrated salt phase change materials employing copper foam as the supporting material
Abstract Thermal conductivity is a crucial factor for selecting appropriate phase change material (PCM) for use in the field of thermal storage. In the current work, sodium acetate trihydrate (SAT) was combined with xanthan gum and copper foam to prepare a composite PCM using a vacuum impregnation method, with the main purpose of increasing its thermal conductivity. The latent heat of SAT/xanthan gum (SAT/X) containing 98 wt% SAT and 2 wt% xanthan gum was measured to be 255.5 J/g, close to the theoretical value according to the content of SAT in the composite SAT/X. The saturated mass fraction of SAT/X in SAT/xanthan gum/copper foam (SAT/X/CF) was calculated to be equal to 77.2%, therefore the SAT/X/CF can have an estimated latent heat of 197.2 J/g. The thermal conductivity of final composite PCM was 2.10 W/(m·K), 1.76 times higher than that of SAT/X, suggesting that copper foam performs well in the area of thermal conductivity enhancement. A heating/cooling cycle was carried out 200 times to examine the cycling stability of SAT/X and SAT/X/CF. The experimental analysis illustrated that the latent heat of SAT/X decreased by only 5.9%, as compared with that of the prepared one. Improved thermal conductivity, high heat storage capacity together with great thermal cycling stability make SAT/X/CF a very promising material in solar thermal energy storage.
09/01/2019 00:00:00
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5.4.6 Salt Hydrates and compositions (Inorganic)
Thermal energy harvest in the discharge of CO2 semi-clathrate hydrate in an emulated cold storage system
Abstract Gas hydrate based cold thermal storage air conditioning applications is a novel technology that arouses interests. Based on a series of studies on the phase change behaviour of a new material, CO 2 gas hydrate with a salt composition of tetra-n-butyl ammonium bromide (TBAB), tetra-n-butyl ammonium fluoride (TBAF) and sodium decyl sulfate (SDS), this work investigates the discharging performance of such a material in a lab-scale cold storage vessel to emulate a practical cold storage air conditioning system. The advantages of this material were found: under 5.5 bar the material has a dissociation temperature of 10.5 °C that is suitable for air conditioning use; 6.5 L cold store enables 0.27 kWh cooling capacity storage in 4 h; CO 2 hydrate cold store is able to offer an adjustable rate of discharge by varying the pressure that is not available in other commonly-used phase change materials. It was also found that the rate of discharge could be improved by increasing the chilled water return temperature. However, the low pressure condition is still a restraint of hydrate formation; besides, both CO 2 –TBAB hydrate and TBAB hydrate form simultaneously in the vessel under low pressures. It requires further investigations to enhance the formation of CO 2 –TBAB hydrate in the cold store, especially under low pressures.
09/01/2017 00:00:00
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5.4.7 Salt Hydrates and compositions (Inorganic)
Thermochemical energy storage
A thermal energy storage medium comprising a hydrophilic polysaccharide supporting an inorganic salt that is capable of transforming from one phase to a less hydrated phase absorbing latent heat, and releasing this latent heat upon the reverse transformation. The polysaccharide, preferably Xanthan Gum, may be incorporated in concentrations of 0.05% to 3% together with a nucleating agent in order to form a material that transforms when cooled back to the transformation temperature, or in greater concentrations of 1% to 5% without a nucleating agent to form a material that may be cooled below the transformation temperature without transformation taking place, and stored at ambient temperature while still storing the latent heat until activated. The medium is gelled in the less hydrated phase and in some embodiments the gel is pseudoplastic thus enabling it to be poured into chambers of an energy storage device, and then regain its original viscosity at rest.
08/03/1983 00:00:00
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5.5 Eutetic phase change materials

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Organic and Eutectic phase change material operate on the same principle as inorganic (as salt) PCM. Research on these components has mostly been initiated by some obvious disadvantages of salt PCM, such as being corrosive, being incompatible with several materials, experiencing supercooling and segregation during phase transition under thermal cycling. A large number of organic PCMs are available in the temperature range from −5 °C to 190 °C. Depending on the type of applications, the organic PCMs should first be selected based on their phase change temperature. Materials that exhibit phase change below 15 °C are used in cooling applications, while materials that have phase change above 90 °C are used for absorption refrigeration. The organic PCMs and their mixtures that show phase change around 18–65 °C are suitable for the thermal comfort applications in textiles and in buildings. Advantages of eutectics of organic and inorganic compounds: * Eutectics a sharp melting temperature and can be similar to the pure compound * The volumetric storage density is slightly lower than organic PCMs Disadvantages of eutectics of organic and inorganic compounds: \-Relatively new to thermal storage applications, lack of data on their thermo-physical properties ***Applications:*** * Building * Textile * Shipping/Transport

5.5.1 Eutetic phase change materials
Evaluation of a seasonal storage system of solar energy for house heating using different absorption couples
Abstract In this paper, an innovative concept is presented for a long-term energy storage system for house heating, using the absorption process. The solar energy is stored during summer through desorption and the heat is released during winter through absorption. The originality of this concept is to allow the solution to reach the crystallization point, which is usually avoided in the absorption refrigeration machines. The storage capacity and efficiency of seven absorption couples, CaCl 2 /H 2 O, Glycerin/H 2 O, KOH/H 2 O, LiBr/H 2 O, LiCl/H 2 O, NaOH/H 2 O and H 2 O/NH 3 , as a function of the temperature of absorption, temperature of evaporation, temperature of the solution before absorption and the presence of crystals in the storage tank have been studied in this paper. The appearance of crystals increases the storage capacity. The storage capacity increases with the temperature of evaporation and the temperature of the solution before absorption but decreases with the temperature of absorption.
06/01/2011 00:00:00
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5.5.2 Eutetic phase change materials
Investigation of high capacity heat energy storage for building applications
The problems of excessive consumption of fossil resources, oil shortages and greenhouse gas emissions are becoming increasingly severe. Research and development work on new methods of thermal energy storage are imminently required. To effectively store seasonal renewable energy, a novel high capacity heat storage system has been designed and evaluated/validated through laboratory experiments and numerical simulations in this research. The system is driven by direct flow evacuated tube solar collector with enhanced PCM tank and intends to be applied in residential and commercial buildings. Theoretical and experimental approaches and numerical analysis have been employed in this study. Firstly, phase change materials (PCM) with specific heat density, melting point, melting and solidifying time have been investigated. This type of PCMs can maintain a considerable high internal temperature of environment chamber in a frozen ambient temperature. Numerical modelling has been conducted on a passive house (Nottingham H.O.U.S.E) to study whether proposed thermochemical materials can cover relative heating load and be power by solar panel in terms of roof size. Meanwhile, PCMs have been used to give a long duration for temperature-controlled chamber in laboratory, and thermochemical materials have been utilized in closed pumping pipe system for cooling and heating purpose. Secondly, characteristic experiments have been conducted on a modified solar collector working with an enhanced PCM tank that is integrated with a fan coil heat exchanger. The results show that light radiation of tungsten lamps (as a solar simulator) has approximately 70% efficiency to equate to solar radiation under the same Pyranometer reading value. At the same time, the solar system can supply over 50°C heating energy and the PCM tank within it can supply higher output temperature with longer duration than water tank. The efficiency of the whole solar collector heating system is over 50% as a heat absorption chamber in sunny days, while only approximately 10% under mostly cloudy weather. Lastly, proposed thermochemical materials (silica gel, calcium chloride, zeolite 13x, vermiculite and activated carbon) have been evaluated on designed thermochemical absorption chamber to supply fresh high temperature air for space heating. The results show that zeolite holds the highest reacted temperature (over 58°C) and vermiculite has really fast absorbing hydration duration, less than half hour. Silica gel possesses the biggest water absorbing capacity and vermiculite has a worse result. A comparison between experimental and numerical modelling results has been revealed. Considering the complexity of processes in cooling and heating system, the agreement of simulation and experimentation is satisfactory, thus the lumped numerical model is acceptable and significant for investigation of this scaled seasonal high capacity heat storage system. A full size seasonal heat storage system with a nominal heating capacity of 3kW has been proposed and illustrated in economic and environmental issues section. The results from net present value (NPV) and internal rate of return (IRR) sensitivity analysis both shows it is greatly attractive to develop this novel system for application in both household and commercial buildings in consideration of its about 9 years payback period, 20 years life span and zero gas (C02) emissions. An intelligent transpired solar collector system is also introduced and illustrated as future work.
07/09/2014 00:00:00
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5.5.3 Eutetic phase change materials
Low-cost, shape-stabilized fly ash composite phase change material synthesized by using a facile process for building energy efficiency
Abstract With increasing building energy consumption, the use of phase change materials (PCMs) to store energy becomes particularly important. However, relatively complex packaging technology, high cost and unstable thermal performance constrain the use of PCMs in the field of building energy efficiency. In this study, co-soluble hydrous salt/fly ash composite PCMs (FA composite PCMs) were prepared by straight dipping using the relatively inexpensive sodium sulfate dehydrate (Na 2 SO 4 ·10H 2 O) as the primary phase change energy storage agent and solid waste fly ash (FA) as a carrier material. The FA composite PCMs were fabricated with an optimal mass ratio of PCMs: FA = 1.7:1. The PCMs' chemical characteristics, morphology and thermal properties were systematically detected. It is shown that PCMs adsorbed to FA belong to physical adsorption according to FTIR and XRD analysis results. Confined in the microspores of fly ash, the phase separation phenomenon of FA composite PCMs is largely eliminated, and its undercooling has also been a certain degree of relief. In addition, the FA composite PCMs exhibit good thermal properties; for example, the latent heat reaches 106.9 J/g with a melting temperature of 25.3 °C and remains at 87.1 J/g even after 100 thermal cycles. Moreover, the FA composite PCMs exhibit excellent environmental sustainability evaluated using a new simple approach. Finally, no leakage was observed in the FA composite PCMs during the solid-liquid phase transition.
01/01/2019 00:00:00
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5.5.4 Eutetic phase change materials
Methods and Systems of Regenerative Heat Exchange
The present disclosure teaches apparatuses, systems, and methods for improving energy efficiency using high heat capacity materials. Some embodiments include a phase change material (PCMs). Particularly, the systems may include a re-gasification system, a liquefaction system, or an integrated system utilizing a heat exchanger with a regenerator matrix, a shell and tube arrangement, or cross-flow channels (e.g. a plate-fin arrangement) to store cold energy from a liquefied gas in a re-gasification system at a first location for use in a liquefaction process at a second location. The regenerator matrix may include a plurality of PCMs stacked sequentially or may include a continuous phase material comprised of multiple PCMs. Various encapsulation approaches may be utilized. Reliquefaction may be accomplished with such a system. Natural gas in remote locations may be made commercially viable by converting it to liquefied natural gas (LNG), transporting, and delivering it utilizing the disclosed systems and methods.
12/15/2009 00:00:00
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5.5.5 Eutetic phase change materials
Recent research on conductive phase-change materials for energy storage
(PCM) for energy storage are materials that can store and release thermal energy through melting and solidification processes. Over the years a fair amount of work has been done to determine the suitability and properties of such materials. The first challenge was to find ways to prevent the leaking or flow of the molten paraffins. Some solutions e.g. encapsulation of the PCM by a thin polymeric shell and the formation of immiscible polymer/ PCM blends were investigated. The most recently investigated challenge is to improve the thermal conductivity of the systems, because both polymer and paraffin have relatively high thermal resistivities. A few papers were published during the past four years where the PCM was directly mixed with the conductive filler. These investigations included expanded graphite, carbon nanofibres and carbon nanotubes as fillers mixed into several paraffinbased PCMs. Generally the thermal conductivity increased, but several factors such as particle shape and orientation and particle dispersion were found to influence the extent of improvement in thermal conductivity. Another approach was the microencapsulation of a PCM by an inorganic conductive shell. The most investigated approach was the impregnation of thermally conductive, porous fillers with the liquid PCM. It was observed that the PCM was trapped inside the pores of the fillers, and generally no leakage was observed after melting of the PCM. The last approach, which involves polymers, is the formation of immiscible polymer/PCM blends containing conductive fillers. The effectiveness of such systems is determined by the extent of immiscibility of the polymer and PCM, and the strength of the interaction between the polymer or PCM and the conductive filler. To me the last approach is the most interesting from a polymer scientist’s viewpoint, because there are a number of factors that may determine the properties and effectiveness of such a phase-change system, e.g. crystallization kinetics of polymer and PCM, extent of co-crystallization, location and dispersion of conductive filler particles, extent of interaction of the filler particles with respectively the polymer and the PCM, to name a few. This may not be groundbreaking research, but the results of such research will certainly contribute to the finding of solutions for the provision of renewable energy.
01/01/2013 00:00:00
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5.6 Ice/Water

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Seasonal cold storage is a highly efficient and environmentally friendly technique that uses the stored natural cold energy in winter (e.g., snow, ice or cold ambient air) for free cooling in summer. Ice storage air conditioning is the process of using ice for thermal energy storage. This is practical because of water's large heat of fusion: one metric ton of water (one cubic metre) can store 334 megajoules (MJ) (317,000 BTU) of energy, equivalent to 93 kWh (26.4 ton-hours). The charged cold energy is stored in the form of ice in an insulated tank and is extracted as chilled water for cooling supply in summer, which helps to reduce the chiller running time and reduce the associated electricity consumption and greenhouse gas emission significantly. ***Applications:*** * Air conditioning * Gas turbine air inlet cooling

5.6.1 Ice/Water
A seasonal cold storage system based on separate type heat pipe for sustainable building cooling
Seasonal cold storage is a high-efficient and environmental-friendly technique that uses the stored natural cold energy in winter (e.g., snow, ice or cold ambient air) for free-cooling in summer. This paper presents a seasonal cold storage system that uses separate type heat pipes to charge the cold energy from ambient air in winter automatically, without consuming any energy. The charged cold energy is stored in the form of ice in an insulated tank and is extracted as chilled water for cooling supply in summer, which help to reduce the chiller running time and reduce the associated electricity consumption and greenhouse gas emission significantly. A quasi-steady two-dimensional mathematical model of the system is developed for characterizing the dynamic performance of ice growth (i.e., cold charging). The model is validated using the field measurement data from an ice charging experiment conducted in Beijing. The impacts of various affecting factors, including the weather data and the key parameters of heat pipes, on the charging performance of the cold storage system are analyzed. The effectiveness and sustainability of the proposed system for cooling are demonstrated through a case study of a kindergarten building in Beijing.
01/01/2016 00:00:00
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5.6.2 Ice/Water
Experimental study of water solidification phenomenon for ice-on-coil thermal energy storage application utilizing falling film
Abstract In summer season, peak load occurs due to high cooling demand during warmest hours. Thus, cold energy storage systems are used to store energy when it is abundant to reduce electrical energy consumption for cooling during peak load time. Thermal energy can be stored using either sensible or latent heat through phase change materials (PCMs). Ice-on-coil is a common method for thermal energy storage, but its heat transfer rate decreases during charging due to the low thermal conductivity of ice. The system considered here is a dynamic direct ice-making storage unit that utilizes the high heat transfer coefficient of falling film when it falls on the outside of the tube surface in the form of discrete droplets, jets, or a continuous sheet depending on the flow rate. Five parallel circular tubes subjected to different modes of the falling film were tested for formation of ice after being fed internally by cold ethylene-glycol solution. The accumulated ice was measured by recording the changes in weight of the tubing system during the duration of each experiment using an electronic scale. About 1.73 g/m 2  s of ice was formed on the tubing with a starting heat transfer coefficient of 170 W/m 2  K when the falling film was in the jet mode. The information gained here is presented as design factors that can be used to improve the performance of ice-dependent thermal energy storage systems using PCM.
01/01/2019 00:00:00
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6. Latent Integration technologies

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Technologies to integrate Phase Change Materials into processes.


6.1 Building materials filled with PCM

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The applications of PCMs in the construction industry are endless. They can be incorporated into every element of a building, from the roof to the floors to electrical appliances. They can be used to reduce rapid temperature fluctuations within internal environments by storing latent heat in the solid-liquid phase change of a material. Heat is absorbed and released almost isothermally, and is used to reduce the energy consumed by conventional heating and cooling systems by reducing peak loads. ***Examples:*** * The incorporation of PCMs into building envelope solutions takes advantage of solar energy, contributing to the overall reduction of energy consumption associated to use of the air conditioning systems * Use of phase change materials (PCM) in concrete pavements to store heat, which can be used to reduce ice formation and snow accumulation on the surface of the concrete pavement. ***Applications:*** * Domestic * Industrial

6.1.1 Building materials filled with PCM
Evaluating the Use of Phase Change Materials in Concrete Pavement to Melt Ice and Snow
AbstractThis paper investigates the potential use of phase change materials (PCM) in concrete pavements to store heat, which can be used to reduce ice formation and snow accumulation on the surface of the concrete pavement. The thermal properties of the PCMs are evaluated using a low-temperature differential scanning calorimeter (LT-DSC) while a longitudinal guarded comparative calorimeter (LGCC) is used to evaluate the thermal response of cementitious mortar containing the PCM. Paraffin oil (petroleum based) and methyl laurate (vegetable based) were selected as PCMs since they have high enthalpies of fusion (∼130–170  J/g) and have desirable freezing temperatures (∼2–3°C) during the liquid to solid phase transformation. Two approaches were used to place the PCM in the mortar specimens: (1) placing the PCM in lightweight aggregate (LWA) in mortar and (2) placing the PCM in an embedded tube that is placed in mortar. The durability and stability of the PCMs in the cementitious system were studied by monitor...
04/01/2016 00:00:00
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6.1.2 Building materials filled with PCM
Experimental testing and numerical modelling of masonry wall solution with PCM incorporation: A passive construction solution
Abstract Presently the essential research trend for sustainable buildings is the use of renewable energy sources and the development of new techniques of energy storage. Phase change materials (PCMs) may store latent heat energy in addition to the typical sensible energy capacity of current building materials, allowing to store significantly more energy during the phase change process (solid to liquid and vice versa). The incorporation of PCMs into building envelope solutions takes advantage of solar energy, contributing to the overall reduction of energy consumption associated to use of the air conditioning systems. This paper presents and discusses research developed in two main components: experimental testing and numerical simulation of a building component with PCM incorporation. The main goal of the experimental testing carried out was to evaluate the effect of the incorporation of PCM macro encapsulated into a typical Portuguese clay brick masonry enclosure wall. It is evaluated the influence of the phase change process of the PCM over the attenuation and time delay of the temperature fluctuations for indoor spaces. The experimental results allowed the calibration and validation of the numerical model, enabling to carry out parametric studies with different PCMs quantity analysing consequent temperature damping and time delay.
06/01/2012 00:00:00
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6.1.3 Building materials filled with PCM
Heat Storage in Future Zero-Energy Buildings
Institute of Materials & Machine Mechanics of Slovak Academy of Sciences (IMSAS) possesses the unique experience in the field of production of heating/cooling wall and ceiling panels based on aluminium foams for future energy autonomous houses and buildings. These novel heating/cooling panels have been developed and successfully tested in pilot application in 260 m2 open space office room. The low heat capacity of aluminium foam allows changing the temperature very quickly, whereas the temperature of the entire foam volume is always very uniform due to excellent thermal conductivity of aluminium cell walls. The heat is dissipated by foam using foamed-in tubes, which are completely embedded in the foam, keeping excellent contact to cell wall aluminium. Good thermal conductivity of the foam resulted in short length of embedded tubes, what is beneficial for low flow resistance and necessary pumping systems. The foamed panels can be partially impregnated at facing side by appropriate plaster, which improves the appearance and also serves as an absorber of potentially condensed air humidity. The developed panels provide an excellent alternative for large built-in ceiling radiators for efficient heating or cooling of rooms using low potential energy resources. The most appropriate ways of using these panels, which are able to increase extremely energy-efficiency in buildings have been outlined in this contribution. Moreover, technological solutions based on ability to store solar thermal energy effectively within the energy efficient buildings are introduced to scientific community in this contribution. The local thermal energy storage must provide the required flexibility to match the heat demand and supply because thermal energy cannot be transported over long distances without significant losses. Solar heat supply fluctuates not only between day and night, but extremely high fluctuations are problematically solvable mainly between summer and winter. In order to use the energy from sun to its maximum, the storage should be capable not only for short periods (hours and days) but also for long-term, e.g. seasonal heat storage. The advanced technologies for short-term storage as well as seasonal storage of solar heat obtained by thermo-solar collectors which allow to reduce energy consumption significantly during winter by interior heating and hot water generation in energyefficient buildings are discussed in this study.
01/01/2015 00:00:00
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6.1.4 Building materials filled with PCM
Integrating phase change materials in construction materials: Critical review
Abstract Applications of phase change materials (PCMs) have become of great interest in recent years owing to beneficial effects on the thermal, mechanical and durability properties of construction and pavement materials. PCMs can alter the thermal mass and thermal inertia of building materials, thus enhancing thermal energy storage. The effects of PCMs on cement hydration, thermal stress and shrinkage of concrete have stimulated further applications. Despite various virtues of PCMs in construction and pavement materials, their drawbacks still need concerted research efforts. Among the fundamental problems of PCMs is their risk of leakage in the melted state. Hence, several techniques have been proposed to mitigate this problem. The present study examines potential methods of incorporating PCMs into building materials, including microencapsulation, macro-encapsulation, shape-stabilization, and porous inclusion. A critical analysis of PCM applications and stabilization materials and methods in concrete is provided, hence identifying practical recommendations, research needs and current knowledge gaps.
08/01/2019 00:00:00
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6.1.5 Building materials filled with PCM
Numerical and experimental study on the use of microencapsulated phase change materials (PCMs) in textile reinforced concrete panels for energy storage
Abstract The present work focuses on the development of facade elements for improvement of energy efficiency in buildings. The proposed solution consists of new textile reinforced concrete panels including microencapsulated phase change materials (PCMs) in a variety of mix designs. A multiscale experimental characterization was performed to evaluate the thermal performance of different configurations. The results showed an increase in heat storage capacity and thermal inertia of the textile reinforced concrete with PCMs. In addition, A numerical model was developed and validated with experimental results.
08/01/2018 00:00:00
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6.1.6 Building materials filled with PCM
Thermal properties of lightweight concrete incorporating high contents of phase change materials
Abstract This research investigated the latent heat and energy storage of lightweight concrete containing high contents of phase change material (PCM) (up to about 7.8% by weight of concrete). PCM – Polyethylene Glycol (PEG) with a fusion temperature of approximately 42–46 °C was impregnated into porous lightweight aggregates up to 24% by weight. The PCM aggregates were then used to replace normal lightweight aggregate at a rate of 0, 25, 50, 75 and 100% by volume. The samples were subjected to series of experiments such as compressive strength (EN12390-3 2002), flexural strength (ASTM C78 ), thermal conductivity (ASTM C518 ) and the thermal storage of phase change materials examined using a heat flow meter apparatus (ASTM C1784 ) at the age of 28 days. Results show that the existence of PCM aggregates affects both mechanical and thermal properties of concrete to different degrees. The mechanical properties appear to improve with increasing PCM aggregate content. For thermal properties such as thermal conductivity and specific heat, the state of the PCM (liquid or solid state) as well as the testing temperature during the test, show significant influence on the obtained results. The latent heat was found to increase proportionally with the increasing PCM aggregate replacement rate.
05/01/2019 00:00:00
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6.2 Phase Change Material in water tanks

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In recent years, latent heat storage systems have been increasingly used in building energy conservation, solar heating systems, and waste heat recovery systems. The water tank as a key component of solar heating systems has been widely applied in practical applications. ***Applications:*** * Solar heating systems * Domestic

6.2.1 Phase Change Material in water tanks
Heat transfer enhancement in water when used as PCM in thermal energy storage
Efficient and reliable storage systems for thermal energy are an important requirement in many applications where heat demand and supply or availability do not coincide. Heat and cold stores can basically be divided in two groups. In sensible heat stores the temperature of the storage material is increased significantly. Latent heat stores, on the contrary, use a storage material that undergoes a phase change (PCM) and a small temperature rise is sufficient to store heat or cold. The major advantages of the phase change stores are their large heat storage capacity and their isothermal behavior during the charging and discharging process. However, while unloading a latent heat storage, the solid–liquid interface moves away from the heat transfer surface and the heat flux decreases due to the increasing thermal resistance of the growing layer of the molten/solidified medium. This effect can be reduced using techniques to increase heat transfer. In this paper, three methods to enhance the heat transfer in a cold storage working with water/ice as PCM are compared: addition of stainless steel pieces, copper pieces (both have been proposed before) and a new PCM-graphite composite material. The PCM-graphite composite material showed an increase in heat flux bigger than with any of the other techniques.
07/01/2002 00:00:00
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6.2.2 Phase Change Material in water tanks
Review on application of phase change material in water tanks
Latent heat storage with phase change material is a superior way of storing thermal energy because of its high thermal storage density, isothermal nature of the storage process, and easy control. In recent years, latent heat storage systems have been increasingly used in building energy conservation, solar heating systems, and waste heat recovery systems. The water tank as a key component of solar heating systems has been widely applied in practical applications. This article first reviews the research on the water tank integrated with phase change material in terms of existing research methods and heat transfer enhancing technologies and then summarizes the applications of various phase change material–based water tanks. Finally, the further research suggestions on the phase change material–based water tank are proposed in this article. The successful completion of this review will not only deepen the understanding on the research development of phase change material–based water tank but also promote pra...
07/01/2017 00:00:00
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6.3 Bed Storage concept

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High heat transfer coefficients can be achieved between a fluidized bed of coated PCM particles and a heat exchanging surface: heat can be captured by the particulate gas–solid flowing suspension. ***Example of installations:*** * Packed beds: Air is used as heat transfer fluid (HTF) flowing in an annular shell outside the bed for charging and discharging the bed. The bed is filled with CaO/Ca(OH)₂ powders with particles diameter of the order 5μm. * Fluidized beds: a novel technique which utilises solids transfer between adjacent fluidized beds by means of jet jumps for recovering and/or storing waste heat. Results showed that the fluidized bed heat exchanger effectiveness approached 80% of a perfect parallel flow heat exchanger. The effectiveness increased with increasing jet pump flowrate, fluidizing velocity and by the use of vertical baffles. * Moving bed: Moving Bed Heat Exchanger MBHX storage concept for CSP systems using sensible heat transfer medium aims at using a low cost solid storage media. This concept requires intermediate bulk cycles to transfer heat between the solar field and the storage material (the bulk). ***Applications:*** * Low temperature industrial heat * Solar concentrator

6.3.1 Bed Storage concept
Analysis of blow-air amount for fixed bed gasifier
Through analysis of basic principle and process forming high temperature zone in oxidizing layer and intermediate layer in phase of blowing air in fixed bed gasifier,it is revealed the features of temperature in gasifing layer and their effect on reaction and coke consumption.The suitable ammout of blow-air is proposed by storing maxmum heat in gasifier with solid coal and releasing minimam heat out of gasifier.
01/01/2004 00:00:00
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6.3.2 Bed Storage concept
Forced convection adsorption cycle with packed bed heat regeneration
Abstract The convective thermal wave is part of a patented cycle which uses heat transfer intensification to achieve both high efficiency and small size from a solid adsorption cycle. Such cycles normally suffer from low power density because of poor heat transfer through the adsorbent bed. Rather than attempting to heat the bed directly, it is possible to heat the refrigerant gas outside the bed and to circulate it through the bed in order to heat the sorbent. The high surface area of the grains leads to very effective heat transfer with only low levels of parasitic power needed for pumping. The new cycle presented here also utilises a packed bed of inert material to store heat between the adsorption and desorption phases of the cycle. The high degree of regeneration possible leads to good coefficients of performance (COPs). Thermodynamic modelling, based on measured heat transfer data, predicts a COP (for a specific carbon) of 0.90 when evaporating at 5°C and condensing at 40°C, with a generating temperature of 200°C and a modest system regenerator effectiveness of 0.8. Further improvement is possible. Experimental heat transfer measurements and cycle simulations are presented which show the potential of the concept to provide the basis of a gas-fired air conditioner in the range 10–100 kW cooling. A research project to build a 10-kW water chiller is underway. The laboratory system, which should be operational by June 1997, is described.
01/01/1999 00:00:00
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6.3.3 Bed Storage concept
High Temperature Thermochemical Energy Storage Using Packed Beds
Thermal energy storage units are vital for development of the efficient solar power generation systems due to fluctuating nature of daily and seasonal solar radiations. Two available efficient and practical options to store and release solar energy at high temperatures are latent heat storage and thermochemical storage. Latent heat storage can operate only at single phase change temperature. This problem can be avoided by some of the thermochemical storage systems in which solar energy can be stored and released over a range of high temperature by endothermic and exothermic reactions. One such reaction system is reversible reaction involving dehydration of Ca(OH)2 and hydration of CaO. This system is considered in the present study to model a circular fixed bed reactor for storage and release of heat at high temperatures. Air is used as heat transfer fluid (HTF) flowing in an annular shell outside the bed for charging and discharging the bed. The bed is filled with CaO/Ca(OH)2 powders with particles diameter of the order 5μm. Three dimensional transient model has been developed and simulations are performed using finite elements based COMSOL Multiphysics. Conservation of mass and energy equations, coupled with reaction kinetics equations, are solved in the three dimensional porous bed and the heat transfer fluid channel. Parametric study is performed by varying HTF parameters, bed dimensions and process conditions. The results are verified through a qualitative comparison with experimental and simulation results in the literature for similar geometric configurations.Copyright © 2016 by ASME
11/11/2016 00:00:00
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6.3.4 Bed Storage concept
Innovative sensible heat transfer medium for a moving bed heat exchanger in solar central receiver power plants
Renewable energies are gaining importance due to the steadily increasing scarcity of fossil fuels, the ongoing climate change and last but not least the risks which accompany the use of nuclear power. In this growing market, solar thermal power plants offer a centralized, potentially load following electricity production. To serve this need, the integration of thermal energy storage systems is essential. The Moving Bed Heat Exchanger MBHX storage concept for CSP systems using sensible heat transfer medium aims at using a low cost solid storage media. This concept requires intermediate bulk cycles to transfer heat between the solar field and the storage material (the bulk). Heat Transfer Fluids (HTF) such as synthetic oils (mobiltherm 603) are typically used. In this work, granular materials such as sand and rocks are studied to present an additional HTF to represent an efficient and cost-effective alternative. Low cost solid particulates can store and transport heat at temperatures over 1000°C. For the purpose of heat recovery, a moving bed heat exchanger (MBHX) is applied and tested. In this study, the dense granular mass is gravity-driven through a heat exchanger. The performance of the MBHX with the utilization of Sand, Basalt, and a Mixture of Sand and Basalt as a granular material was experimentally investigated. It is found that the effectiveness of the MBHX using a mixture of 50% sand and 50% basalt improved by 30% compared to using sand alone.
04/01/2017 00:00:00
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6.3.5 Bed Storage concept
Multiple fluidized-bed heat recovery: An investigation
Abstract The overall efficiency of process equipments can be significantly improved by heat recovery from waste gases, the recovered heat being utilised for raising steam, preheating air, etc. This paper reports on developments of a novel technique which utilises solids transfer between adjacent fluidized beds by means of jet jumps for recovering and/or storing waste heat. Results showed that the fluidized bed heat exchanger effectiveness approached 80% of a perfect parallel flow heat exchanger. The effectiveness increased with increasing jet pump flowrate, fluidizing velocity and by the use of vertical baffles. The rate of heat recovery could be easily controlled, by controlling the solid circulation rate. The advantages of the proposed heat exchanger includes, lack of moving parts, freedom from fouling and corrosion, low cross-contamination of gases and it is based on proven technology. Application envisaged is, as a preliminary unit for recovering waste heat from dust contaminated, high temperature exhaust gases.
01/01/1987 00:00:00
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6.3.6 Bed Storage concept
Shell-and-tube or packed bed thermal energy storage systems integrated with a concentrated solar power: A techno-economic comparison of sensible and latent heat systems
Abstract A detailed techno-economic comparison—using annual, transient integrated system modelling—was conducted for sensible and latent heat thermal energy storage (TES) systems. As the most viable near-term competitors, thermocline/packed-bed and shell-and-tube configurations were compared to the conventional two-tank molten salt system. Concrete and a range of phase change materials (PCMs) were considered as the storage mediums in this study. All analyses were conducted for 15 h of storage capacity for the 19.9 MWe Gemasolar concentrated solar power (CSP) plant as a real-world case study. It was found that when the CSP plant is constrained to the operational within the tight bounds of the standard two-tank system, the dual-media thermocline (DMT) system with concrete or encapsulated PCM shows the best performance. Imposing rigid operational boundaries significantly disadvantages shell-and-tube (ST) systems (e.g. resulting in up to ∼50% less annual electricity production than a CSP plant with two-tank system). However, the results of this study reveal that extending the TES charge and discharge cut-off temperatures closer to the plant’s maximum and minimum operating range (i.e. 800 K and 650 K) can maximize the potential of dual-media TES alternatives. Under these loose operational conditions, the CSP plant will be required to occasionally operate at conditions which are far from its nominal design point (i.e. up to 75% variation). This flexibility allows all the TES alternatives considered in this study to achieve similar CSP annual electricity output as the two-tank system. In this case (e.g. all TES systems achieve the same annual output), the TES alternatives can be compared based on their specific costs rather than their levelized cost of electricity. Compared to the specific cost of two-tank molten salt systems, ∼24.5 US$ kWh th −1 , a 62% reduction of specific storage cost was found to be achievable with concrete storage a dual-media thermocline (DMT) system, representing the best techno-economic option. This was followed by 49% cost reduction for a pipeless shell-and-tube (ST) system incorporating concrete or a PCM with 1 mm pipe thickness. Without minimizing the capsule thickness to 0.1 mm, the packed bed system with PCM would never have economic justification. Overall, this study reveals that if CSP systems can be designed to have more flexibility in their operational temperature range, a significant cost savings is available in moving to alternative TES systems.
03/01/2019 00:00:00
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6.4 Heat exchanger integration

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Integration of PCM into heat exchangers. ***Applications:*** * The tanks are connected through a salts-heat transfer fluid heat exchanger, which is coupled to the heat source and the heat sink. * The latent heat TES technology is evaluated in a 0.154 m³ storage tank based on the shell-and-tube heat exchanger concept which is connected to a heat source and a heat sink simulating the waste heat recovery of an industrial process. The material used is 99.5 kg of high density polyethylene (HDPE). * directcontact heat exchanger using erythritol (melting point: 391 K) as a phase change material (PCM) and a heat transfer oil (HTO) for accelerating heat storage

6.4.1 Heat exchanger integration
Cyclic performance of cascaded and multi-layered solid-PCM shell-and-tube thermal energy storage systems: A case study of the 19.9 MWe Gemasolar CSP plant
Abstract A shell-and-tube heat exchanger which incorporates a sensible or phase change material (PCM) as the storage medium offers a potentially commercially viable alternative to the two-tank molten salt system. In particular, cascaded PCMs and multi-layered solid-PCMs (MLSPCMs) were investigated as proposed systems which can reduce the amount of storage material used and ensure optimal storage utilization. In this work, the performance of various thermal energy storage (TES) alternatives integrated into the 19.9 MW e Gemasolar concentrated solar power (CSP) plant (located in Seville, Spain) were compared with the conventional two-tank system. These alternative storage configurations were characterized by a single tank filled with a single, cascaded, or multi-layered storage media. Importantly, as a system-level study, this paper compared the performance of the design alternatives integrated with other CSP components in order to capture the effect of dynamic interactions between the storage system and other CSP components. Through a validated numerical investigation of the annual performance of the integrated systems, all the design alternatives were compared in the context of annual electricity generation, which represents the ultimate criterion to judge the true potential of each alternative. To conduct an apples-to-apples comparison, the storage capacity and geometric parameters were fixed. The design alternatives were categorized based on the storage materials involved and their percentages of occupancy in the TES tank (i.e. 12 storage groups and a total number of 45 design alternatives). It was found that the well-designed TES designs with cascaded PCMs performed similarly in charging and discharging (i.e. with a similar amount of total stored or delivered energy per cycle). This contrasts with a single PCM system, where there exists a significant difference between charging and discharging performance. The results of annual cyclic performance, under real-time operational conditions, indicated that a MLSPCM design configuration that was filled with a high melting point PCM in the top 25% of the tank, sensible concrete in the middle 50%, and a low melting point PCM in the bottom 25% of the tank had the best performance among all design alternatives studied. Moreover, it was found that changing the filler portions any one cascaded PCM group cannot significantly change the annual performance of the system. Contrary to much of the available literature – literature which does not consider system integration – it was shown that the shell-and-tube alternatives can only approach the annual performance of two-tank systems under ‘extended’ operational conditions (i.e. allowing temperature set points to float relatively far away from their fixed design points).
10/01/2018 00:00:00
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6.4.2 Heat exchanger integration
Evaluation of energy density as performance indicator for thermal energy storage at material and system levels
Abstract The increase of the capacity factor of thermal processes which use renewable energies is closely linked to the implementation of thermal energy storage (TES) systems. Currently, TES systems can be classified depending on the technology for storing thermal: sensible heat, latent heat, and sorption and chemical reactions (usually known as thermochemical energy storage). However, there is no standardized procedure for the evaluation of such technologies, and therefore the development of performance indicators which suit the requisites of the final users becomes an important goal. In the present paper, the authors identified the energy density as an important performance indicator for TES, and evaluated it at both material and system levels. This approach is afterwards applied to prototypes covering the three TES technologies: a two-tank molten salts sensible storage system, a shell-and-tube latent heat storage system, and a magnesium oxide and water chemical storage system. The evaluation of the energy density highlighted the difference of its value at the material value, which presents a theoretical maximum, and the results at system level, which considers all the parts required for operating the TES, and thus presents a significantly lower value. Moreover, the proposed approach captured the effect of the complexity and overall size of the system, showing the relevance of this performance indicator for evaluating technologies for applications in which volume is a limiting parameter.
02/01/2019 00:00:00
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6.4.3 Heat exchanger integration
Heat storage in direct-contact heat exchanger with phase change material
Abstract This paper describes the development and performance of a direct-contact heat exchanger using erythritol (melting point: 391 K) as a phase change material (PCM) and a heat transfer oil (HTO) for accelerating heat storage. A vertical cylinder with 200-mm inner diameter and 1000-mm height was used as the heat storage unit (HSU). A nozzle facing vertically downward was placed at the bottom of the HSU. We examined the effects of flowrate and inlet temperature of the HTO using three characteristic parameters of heat storage – difference between inlet and outlet HTO temperatures, temperature effectiveness, and heat storage rate. The temperature history of latent heat storage (LHS) showed three stages: sensible heat of solid PCM, latent heat of PCM, and sensible heat of liquid PCM. Further, the operating mechanism of the DCHEX was proposed to explain the results. The average heat storage rate during LHS was proportional to the increase in flowrate and inlet temperature of HTO. Thus, latent heat can be rapidly stored under large HTO flowrate and high inlet temperature in the DCHEX.
01/01/2013 00:00:00
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6.4.4 Heat exchanger integration
Improved heat storage rate for an automobile coolant waste heat recovery system using phase-change material in a fin–tube heat exchanger
In this study, the actual heat transfer coefficient of a phase-change material (PCM) was measured experimentally with the purpose of improving the heat storage rate of an automotive coolant waste heat storage system using the latent heat of the PCM. The heat transfer rate and time required to store heat was theoretically analyzed in the system where engine coolant was heated by a fin–tube heat exchanger filled with solid PCM. The amount of heat storage necessary for sufficient heating of vehicle coolant was calculated, and the appropriate amount of PCM was determined accordingly. Based on this data, a heat exchanger capable of storing heat under the lowest possible influence of natural convection and conduction thermal resistance of the PCM was designed, and its estimated heat storage rate was calculated. We identified the most effective methods to improve the heat storage rate and efficiency of the PCM-filled heat exchanger.
01/01/2014 00:00:00
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6.4.5 Heat exchanger integration
Shell-and-tube or packed bed thermal energy storage systems integrated with a concentrated solar power: A techno-economic comparison of sensible and latent heat systems
Abstract A detailed techno-economic comparison—using annual, transient integrated system modelling—was conducted for sensible and latent heat thermal energy storage (TES) systems. As the most viable near-term competitors, thermocline/packed-bed and shell-and-tube configurations were compared to the conventional two-tank molten salt system. Concrete and a range of phase change materials (PCMs) were considered as the storage mediums in this study. All analyses were conducted for 15 h of storage capacity for the 19.9 MWe Gemasolar concentrated solar power (CSP) plant as a real-world case study. It was found that when the CSP plant is constrained to the operational within the tight bounds of the standard two-tank system, the dual-media thermocline (DMT) system with concrete or encapsulated PCM shows the best performance. Imposing rigid operational boundaries significantly disadvantages shell-and-tube (ST) systems (e.g. resulting in up to ∼50% less annual electricity production than a CSP plant with two-tank system). However, the results of this study reveal that extending the TES charge and discharge cut-off temperatures closer to the plant’s maximum and minimum operating range (i.e. 800 K and 650 K) can maximize the potential of dual-media TES alternatives. Under these loose operational conditions, the CSP plant will be required to occasionally operate at conditions which are far from its nominal design point (i.e. up to 75% variation). This flexibility allows all the TES alternatives considered in this study to achieve similar CSP annual electricity output as the two-tank system. In this case (e.g. all TES systems achieve the same annual output), the TES alternatives can be compared based on their specific costs rather than their levelized cost of electricity. Compared to the specific cost of two-tank molten salt systems, ∼24.5 US$ kWh th −1 , a 62% reduction of specific storage cost was found to be achievable with concrete storage a dual-media thermocline (DMT) system, representing the best techno-economic option. This was followed by 49% cost reduction for a pipeless shell-and-tube (ST) system incorporating concrete or a PCM with 1 mm pipe thickness. Without minimizing the capsule thickness to 0.1 mm, the packed bed system with PCM would never have economic justification. Overall, this study reveals that if CSP systems can be designed to have more flexibility in their operational temperature range, a significant cost savings is available in moving to alternative TES systems.
03/01/2019 00:00:00
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6.4.6 Heat exchanger integration
The integration of solid-solid phase change material with micro-channel flat plate heat pipe-based BIPV/T
In this paper, the influence of the solid-solid phase change material on the novel micro-channel flat-plate heat-pipe–based building integrated photovoltaic/thermal system has been investigated, which has been expected to store the excess heat, enhance the overall efficiency of the system and maintain the stable photovoltaic temperatures. The proposed system was divided into two parts, i.e. the outdoor part formed by flat-plate glass, photovoltaic panel, micro-channel flat-plate heat pipes, solid-solid phase change material layer and insulated material, and indoor part including the storage tank, water pump and storage batter. The experiments were conducted at the Guangdong University of Technology, China, to investigate the thermal and electrical performance of the proposed system. When the simulated radiation was at 300 W/m2 and water flow rate was at 600 L/h, the maximum average thermal, electrical and overall efficiency were found at 52.9%, 7.9% and 60.8%, respectively, when the xenon lamps were turne...
11/01/2018 00:00:00
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6.5 Macro/ Micro encapsulated PCM

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Encapsulation of PCMs is present in two forms, core-shell and shape-stabilized, depending on the shape of the capsule. Core-shell encapsulation is the term for covering a material (core) with another material (shell), while shape-stabilized encapsulation are composites of PCMs with other materials that retain molten PCMs by capillarity. Micro-encapsulated PCM slurry is a suspension where the PCM is dispersed at 10–20 wt. % without significantly altering the physical properties of the liquid (density, viscosity). Example of micro encapsulation methods: * Emulsion polymerization * In situ polymerization * Interfacial polymerization * Electroplating * Sol-gel process * Mechanical packaging ***Applications:*** * PCM is microencapsulated using a polymeric capsule and dispersed in water. * also used in Slurries and Molten Salt * Since SS-PCMs remain solid, they may also be used to encapsulate SL-PCM’s, which would allow all constituents to contribute to the latent heat storage processes. Similarly, shape stabilized SL-PCMs using SS-PCM matrixes may also offer a viable path. Such approaches could offer cost benefits and higher heat storage capacity. * Used in bedding, building and construction, automotive interiors, clothing and mattresses (see Croda Therm)

6.5.1 Macro/ Micro encapsulated PCM
Effect of internal void placement on the heat transfer performance – Encapsulated phase change material for energy storage
The effect of an internal air void on the heat transfer phenomenon within encapsulated phase change material (EPCM) is examined. Heat transfer simulations are conducted on a two dimensional cylindrical capsule using sodium nitrate as the high temperature phase change material (PCM). The effects of thermal expansion of the PCM and the buoyancy driven convection within the fluid media are considered in the present thermal analysis. The melting time of three different initial locations of an internal 20% air void within the EPCM capsule are compared. Latent heat is stored within an EPCM capsule, in addition to sensible heat storage. In general, the solid/liquid interface propagates radially inward during the melting process. The shape of the solid liquid interface as well as the rate at which it moves is affected by the location of the internal air void. The case of an initial void located at the center of the EPCM capsule has the highest heat transfer rate and thus fastest melting time. An EPCM capsule with a void located at the top has the longest melting time. Since the inclusion of a void space is necessary to accommodate the thermal expansion of a PCM upon melting, understanding its effect on the heat transfer within an EPCM capsule is necessary.
06/01/2015 00:00:00
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6.5.2 Macro/ Micro encapsulated PCM
Numerical and experimental study on the use of microencapsulated phase change materials (PCMs) in textile reinforced concrete panels for energy storage
Abstract The present work focuses on the development of facade elements for improvement of energy efficiency in buildings. The proposed solution consists of new textile reinforced concrete panels including microencapsulated phase change materials (PCMs) in a variety of mix designs. A multiscale experimental characterization was performed to evaluate the thermal performance of different configurations. The results showed an increase in heat storage capacity and thermal inertia of the textile reinforced concrete with PCMs. In addition, A numerical model was developed and validated with experimental results.
08/01/2018 00:00:00
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6.6 Nano PCM

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The main drawback of encapsulated PCMs is their low thermal conductivity, hence the growing interest in dispersing high conductive nanoparticles within the PCMs. Can be made on the same sort of techniques of microcapsulation As an example, different metal nanoparticles were used in order to enhance the thermal conductivity of paraffin wax. ***Applications:*** * Building / HVAC * Passive cooling applications

6.6.1 Nano PCM
Nano-PCMs for enhanced energy storage and passive cooling applications
Abstract It is well known that the heat transfer associated with a phase change process is much higher than sensible enthalpy change even in forced convection. In particular, the vaporization process has been widely studied because it exploits the highest heat transfer coefficient; this heat transfer mechanism is used in both passive (i.e. heat pipes) and active (i.e. refrigerating machines) cooling devices. However, the solid-liquid phase change process is another interesting possibility to reject even high heat loads, especially when they are intermittent. The term Phase Change Materials (PCMs) commonly refers to those materials, which use the solid-liquid phase change process to adsorb and then release heat loads (Mancin et al., 2015). The present work aims at investigating the feasibility of a new challenging use of Aluminum Oxide (Al 2 O 3 ) and Carbon Black (CB) nanoparticles to enhance the thermal properties: thermal conductivity, specific heat, and latent heat of pure paraffin waxes to obtain a new class of PCMs, the so-called nano-PCMs. The nano-PCMs were obtained by seeding 1 wt% of nanoparticles in paraffin waxes with melting temperatures of 20 °C and 25 °C. The thermophysical properties were then measured to understand the effects of the nanoparticles on the thermal properties of both the solid and liquid PCM. These new nano-PCMs can represent a feasible and interesting way to mitigate or eliminate the intrinsic limitations in the use of paraffin waxes as PCMs for both energy storage and passive cooling applications.
01/01/2017 00:00:00
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6.7 Supercooling

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Supercooling, subcooling or undercooling is when a phase change material in liquid state cools down below its melting point without solidifying; leaving it in a metastable state where the latent heat of fusion is not released. In latent heat storage supercooling has traditionally been seen as an undesired effect that had to be avoided as it prevented the heat of fusion from being released when the melting point of the storage material was reached during the discharge process The idea of utilizing supercooled salt hydrates for long term storage has however been known since the late 1920s and pocket-sized heat packs storing heat in supercooled sodium acetate trihydrate were patented in 1978. This principle makes long term thermal energy storage possible by letting the melted salt hydrate remain in supercooled state at ambient temperature in the storage period. Once the heat is needed the solidification of the supercooled solution is triggered and the latent heat of fusion is released as it crystalizes. Investigations have previously shown that there is a potential in utilizing stable supercooling as a storage technique ***Applications:*** * Long term energy house in Danish climatic conditions

6.7.1 Supercooling
Long term thermal energy storage with stable supercooled sodium acetate trihydrate
Abstract Utilizing stable supercooling of sodium acetate trihydrate makes it possible to store thermal energy partly loss free. This principle makes seasonal heat storage in compact systems possible. To keep high and stable energy content and cycling stability phase separation of the storage material must be avoided. This can be done by the use of the thickening agents carboxymethyl cellulose or xanthan rubber. Stable supercooling requires that the sodium acetate trihydrate is heated to a temperature somewhat higher than the melting temperature of 58 °C before it cools down. As the phase change material melts it expands and will cause a pressure built up in a closed chamber which might compromise stability of the supercooling. This can be avoided by having an air volume above the phase change material connected to an external pressure less expansion tank. Supercooled sodium acetate trihydrate at 20 °C stores up to 230 kJ/kg. TRNSYS simulations of a solar combi system including a storage with four heat storage modules of each 200 kg of sodium acetate trihydrate utilizing stable supercooling achieved a solar fraction of 80% for a low energy house in Danish climatic conditions.
12/01/2015 00:00:00
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6.8 Adsorption pump

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The principle of operation of adsorption heat pumps is equal to that of the absorption heat pump. The only difference is that an adsorption heat pump uses solid-sorption instead of the liquid-sorption that is used in absorption systems. The material pairs stated below are regularly applied in adsorption heat pump systems. A study dedicated to an inter-seasonal heat storage process based on novel absorption pump operated in two half-cycles that uses LiBr/H₂O as the absorbent/absorbate couple. The solar energy is stored during summer through desorption, and the heat is released during winter through absorption. A characteristic of the device is that crystallization occurs in the storage tank as its temperature falls under 10 °C at the end of summer or in winter. ***Applications:*** * Domestic

6.8.1 Adsorption pump
Lithium bromide crystallization in water applied to an inter-seasonal heat storage process
Abstract This work is part of a larger study dedicated to an inter-seasonal heat storage process based on novel absorption pump operated in two half-cycles that uses LiBr/H 2 O as the absorbent/absorbate couple. The solar energy is stored during summer through desorption, and the heat is released during winter through absorption. A characteristic of the device is that crystallization occurs in the storage tank as its temperature falls under 10 °C at the end of summer or in winter. Thus, information on the degree of hydration of the crystals at low temperature is required to optimize the storage density. This paper aims to precisely determine the behavior of LiBr in terms of crystallization. In this study, solubility and metastable zone limit curves were assessed using an agitated and thermostated batch crystallizer. A video sensor was employed for assessment of the crystals morphology and thus, the hydrated crystalline forms present inside. The transition temperature between lithium bromide dihydrate and trihydrate was found to be equal to 3.0 °C. The dissolution and crystallization enthalpies were also calculated using the Van׳t Hoff plot, and results were found to be in good agreement with the literature data.
09/01/2015 00:00:00
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6.8.2 Adsorption pump
Simulation der prozessinternen Rückgewinnung von Adsorptionswärmen durch Latentwärmespeicher
Latentwarmespeicher ermoglichen die latente Speicherung groser Warmemengen durch einen Phasenwechsel bei konstantem Temperaturniveau. Die beim Einsatz von Amin-funktionalisierten Adsorbentien zur CO2-Adsorption hohe freiwerdende Adsorptionswarme, die zu einer Minderung der Gleichgewichtskapazitat fuhrt, kann so gespeichert und bei der Desorption in einer Vakuumwechseladsorption wieder zur Regeneration des Adsorbens zur Verfugung gestellt werden. Die Integration verringert Temperaturschwankungen und macht den Prozess effizienter, wobei durch unterschiedliche Lokalisierung der Phasenwechselmaterialien im Adsorber die Effizienzsteigerung beeinflusst werden kann. Phase change materials are able to store heat through a liquefaction phase change at a predetermined temperature. When using amine-functionalised adsorbents for CO2 removal, the excess adsorption heat leads to a decrease in equilibrium capacity, which can thus be mitigated by storing the heat for adsorbent regeneration during the desorption step in a vacuum swing adsorption. This integration diminishes the temperature variations and renders the process more efficient, whereat the exact integration strategy has a strong influence on the overall efficiency of the phase change material performance.
02/01/2014 00:00:00
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6.9 Steam integration

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Integration in a steam cycle ***Examples of applications:*** * The low thermal conductivity of PCM is enhanced by using extended aluminum fins that are attached to the baking plate and extruded inward to the storage. In this paper, twophase loop thermosyphon of steam is used to manage the long distance heat transportation required between the receiver (outside) and the storage (inside a house). The steam in the thermosyphon flow has restricted to a maximum working temperature of 250 °C. Steam is selected for its highest heat capacity, availability and stable nature. It carries heat from the collector focus point and condenses in a coiled pipe imbedded in aluminum plate placed on top of the storage. * A threepart storage system is proposed where a phase change material (PCM) storage will be deployed for the twophase evaporation, while concrete storage will be used for storing sensible heat, i.e. for preheating of water and superheating of steam. A storage system with a total storage capacity of approx. 1 MWh is described, combining a PCM module and a concrete module. The storage modules have been constructed for testing in a DSGtest facility specially erected at a conventional power plant of Endesa in Carboneras (Spain). ***Applications:*** * Cooking * Industrial plants * Concentrated solar power

6.9.1 Steam integration
PCM Storage System with Integrated Active Heat Pipe
Abstract The use of the latent heat of phase change materials (PCM) is considered a promising approach to store heat at a nearly constant temperature for direct steam generation (DSG), but the poor thermal conductivity of commonly available storage materials imposes severe limitations on storage performance. A new method is proposed to overcome the limitations of the low thermal conductivity. The approach is to physically decouple the evaporator pipes from the PCM, thus allowing independent sizing of each component. The thermal link between the two components is done via evaporation and condensation of a heat transfer fluid (HTF), according to the principle of a heat pipe. Pumping the liquid HTF provides active control of the heat pipe operation. The new concept is modeled and compared to the conventional design of conduction based PCM annulus around the steam pipe. An example case shows a significant advantage in performance of the active heat pipe configuration due to its reduced thermal resistance.
01/01/2014 00:00:00
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6.9.2 Steam integration
Steam-based charging-discharging of a PCM heat storage
Latent heat storage and efficient heat transport technology helps to utilize the intermittent solar energy for continuous and near isothermal  applications. However, many latent heat storages face challenges of storage charging, heat retaining, and discharging the stored heat. This paper tries to address the challenges of heat transportation and storage charging-discharging issues. The heat transportation from the receiver over some distance, from outside to the kitchen, is carried out with a stainless pipeline and water as heat transfer fluids. However, the  charging-discharging process is carried by conduction method with the help of fins. In addition, the stored heat is retained for about one-two days by using aerogel insulation. The latent heat is stored in a phase change material (PCM), nitrate salt (mixture of 60% NaNO 3 and 40% KNO 3 ), which melts at 222oC and has 109 J/g specific heat of fusion. The storage has the capacity of storing up to 250oC heat and supply this heat isothermally during baking in the liquid-solid phase transition. However, the sensible heat stored in the solid and liquid form of the PCM is used to perform additional applications that do not require uniform heat which includes bread baking, kita (large pancake) baking and water boiling. The low thermal conductivity of PCM is enhanced by using extended aluminum fins that are attached to the baking plate and extruded inward to the storage. In this paper, two-phase loop thermosyphon of steam is used to manage the long distance heat transportation required between the receiver (outside) and the storage (inside a house). The steam in the thermosyphon flow has restricted to a maximum working temperature of 250oC. Steam is selected for its highest heat capacity, availability and stable nature. It carries heat from the collector focus point and condenses in a coiled pipe imbedded in aluminum plate placed on top of the storage. Many fins are solidly attached to this plate to conduct the heat down to the PCM inside the storage during charging. This design configuration avoids pressure development inside the PCM storage and the charging-discharging temperature is recorded in three zones (top, middle and bottom) of the storage. The experimental and numerical results show that the heat transportation, retention and charging-discharging methods are effective. Keywords : Solar energy, PCM storage, Latent heat storage, Two-phase thermosyphon.
05/17/2018 00:00:00
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6.9.3 Steam integration
Thermal energy storage for direct steam generation
Abstract Parabolic trough power plants with direct steam generation are a promising option for future cost reduction in comparison to the SEGS type technology. These new solar thermal power plants require innovative storage concepts, where the two-phase heat transfer fluid poses a major challenge. A three-part storage system is proposed where a phase change material (PCM) storage will be deployed for the two-phase evaporation, while concrete storage will be used for storing sensible heat, i.e. for preheating of water and superheating of steam. A storage system with a total storage capacity of approx. 1 MW h is described, combining a PCM module and a concrete module. The storage modules have been constructed for testing in a DSG-test facility specially erected at a conventional power plant of Endesa in Carboneras (Spain). Commissioning of the storage system started in May 2010; testing under real steam conditions around 100 bar will begin in August 2010.
04/01/2011 00:00:00
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6.10 Heat pipes filled with PCM

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Integrating PCM with heat pipes. ***Examples:*** * The issue of the low conductivity of PCMs has been addressed by using an embedded finned watercharged heat pipes into the PCM bulk The approach is to physically decouple the evaporator pipes from the PCM, thus allowing independent sizing of each component. * The thermal link between the two components is done via evaporation and condensation of a heat transfer fluid (HTF), according to the principle of a heat pipe. Pumping the liquid HTF provides active control of the heat pipe operation. The new concept is modeled and compared to the conventional design of conduction based PCM annulus around the steam pipe * The adiabatic section of heat pipe is covered by a storage container with phase change material (PCM), which can store and release thermal energy depending upon the heating powers of evaporator and fan speeds of condenser ***Applications:*** * Electronic cooling * Industrial

6.10.1 Heat pipes filled with PCM
A state-of-the-art review on hybrid heat pipe latent heat storage systems
The main advantage of latent heat thermal energy storage systems is the capability to store a large quantity of thermal energy in an isothermal process by changing phase from solid to liquid, while the most important weakness of these systems is low thermal conductivity that leads to unsuitable charging/discharging rates. Heat pipes are used in many applications – as one of the most efficient heat exchanger devices – to amplify the charging/discharging processes rate and are used to transfer heat from a source to the storage or from the storage to a sink. This review presents and critically discusses previous investigations and analysis on the incorporation of heat pipe devices into latent heat thermal energy storage with heat pipe devices. This paper categorizes different applications and configurations such as low/high temperature solar, heat exchanger and cooling systems, analytical approaches and effective parameters on the performance of hybrid HP–LHTES systems.
11/01/2015 00:00:00
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6.10.2 Heat pipes filled with PCM
An investigation into the use of the heat pipe technology in thermal energy storage heat exchangers
Abstract Finding a solution to store industrial wasted heat for later use in order to reduce energy usage has been on the rise in recent years. This paper investigates the capability of latent heat TES (Thermal Energy Storage) system using PCM (Phase Change Material) to store/release a large amount of energy in a small volume compared to sensible heat TES system. In this work, the issue of the low conductivity of PCMs has been addressed by using an embedded finned water-charged heat pipes into the PCM bulk. Both heat pipes and the PCM tank used in this investigation were made of 316 L stainless steel. The PCM used in this work was PLUSICE S89, which has a melting temperature of 89 °C and crystallization point of 77 °C. The evaporator section of the heat pipe was heated by condensing a steam flow. The heat that was absorbed in the evaporator section was then discharged to the PCMs by the heat pipe multi-legged finned condenser. Tests were conducted for both charging (melting) and discharging (crystallization) of PLUSICE S89. It was observed that the thermal resistance posed by PCM during the discharging stage was higher compared to that during the charging process.
10/01/2017 00:00:00
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6.10.3 Heat pipes filled with PCM
PCM Storage System with Integrated Active Heat Pipe
Abstract The use of the latent heat of phase change materials (PCM) is considered a promising approach to store heat at a nearly constant temperature for direct steam generation (DSG), but the poor thermal conductivity of commonly available storage materials imposes severe limitations on storage performance. A new method is proposed to overcome the limitations of the low thermal conductivity. The approach is to physically decouple the evaporator pipes from the PCM, thus allowing independent sizing of each component. The thermal link between the two components is done via evaporation and condensation of a heat transfer fluid (HTF), according to the principle of a heat pipe. Pumping the liquid HTF provides active control of the heat pipe operation. The new concept is modeled and compared to the conventional design of conduction based PCM annulus around the steam pipe. An example case shows a significant advantage in performance of the active heat pipe configuration due to its reduced thermal resistance.
01/01/2014 00:00:00
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6.11 Supercritical fluids with PCM

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On the use of supercritical fluids: ***Example of applications:*** * The use of supercritical fluids allows cost affordable high density storage with a combination of latent heat and sensible heat in the two phase as well as the supercritical state. This technology will enhance penetration of several thermal power generation applications and high temperature water for commercial use if the overall cost of the technology can be demonstrated to be lower than the current state of the art molten salt using sodium nitrate and potassium nitrate eutectic mixtures. * he volumetric energy density of a singletank supercritical fluid energy storage system is significantly higher than a twotank molten salt energy storage system due to the high compressibilities in the supercritical state. As a result, the singletank energy storage system design can lead to almost a factor of ten decrease in fluid costs. ***Applications:*** * Concentrated solar power plants

6.11.1 Supercritical fluids with PCM
A 5 kWht Lab-Scale Demonstration of a Novel Thermal Energy Storage Concept With Supercritical Fluids
An alternate to the two-tank molten salt thermal energy storage system using supercritical fluids is presented. This technology can enhance the production of electrical power generation and high temperature technologies for commercial use by lowering the cost of energy storage in comparison to current state-of-the-art molten salt energy storage systems. The volumetric energy density of a single-tank supercritical fluid energy storage system is significantly higher than a two-tank molten salt energy storage system due to the high compressibilities in the supercritical state. As a result, the single-tank energy storage system design can lead to almost a factor of ten decrease in fluid costs. This paper presents results from a test performed on a 5 kWht storage tank with a naphthalene energy storage fluid as part of a small preliminary demonstration of the concept of supercritical thermal energy storage. Thermal energy is stored within naphthalene filled tubes designed to handle the temperature (500 °C) and pressure (6.9 MPa or 1000 psia) of the supercritical fluid state. The tubes are enclosed within an insulated shell heat exchanger which serves as the thermal energy storage tank. The storage tank is thermally charged by flowing air at >500 °C over the storage tube bank. Discharging the tank can provide energy to a Rankine cycle (or any other thermodynamic process) over a temperature range from 480 °C to 290 °C. Tests were performed over three stages, starting with a low temperature (200 °C) shake-out test and progressing to a high temperature single cycle test cycling between room temperature and 480 °C and concluding a two-cycle test cycling between 290 °C and 480 °C. The test results indicate a successful demonstration of high energy storage using supercritical fluids.Copyright © 2013 by ASME
07/14/2013 00:00:00
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6.11.2 Supercritical fluids with PCM
High Density Thermal Energy Storage With Supercritical Fluids
A novel approach to storing thermal energy with supercritical fluids is being investigated, which if successful, promises to transform the way thermal energy is captured and utilized. The use of supercritical fluids allows cost-affordable high-density storage with a combination of latent heat and sensible heat in the two-phase as well as the supercritical state. This technology will enhance penetration of several thermal power generation applications and high temperature water for commercial use if the overall cost of the technology can be demonstrated to be lower than the current state-of-the-art molten salt using sodium nitrate and potassium nitrate eutectic mixtures. An additional attraction is that the volumetric storage density of a supercritical fluid can be higher than a two-tank molten salt system due to the high compressibilities in the supercritical state.This paper looks at different elements for determining the feasibility of this storage concept — thermodynamics of supercritical state with a specific example, naphthalene, fluid and system cost and a representative storage design. A modular storage vessel design based on a shell and heat exchanger concept allows the cost to be minimized as there is no need for a separate pump for transferring fluid from one tank to another as in the molten salt system. Since the heat exchangers are internal to the tank, other advantages such as lower parasitic heat loss, easy fabrication can be achieved.Results from the study indicate that the fluid cost can be reduced by a factor of ten or even twenty depending on the fluid and thermodynamic optimization of loading factor. Results for naphthalene operating between 290 °C and 475 °C, indicate that the fluid cost is approximately $3/kWh compared with $25-$50/kWh for molten salt. When the storage container costs are factored in, the overall system cost is still very attractive. Studies for a 12-hr storage indicate that for operating at temperatures between 290–450 °C, the cost for a molten salt system can vary between $66/kWh to $184/kWh depending on molten salt cost of $2/kg or a more recent quote of $8/kg. In contrast, the cost for a 12-hr supercritical storage system can be as low as $40/kWh. By using less expensive materials than SS 316L, it is possible to reduce the costs even further.© 2012 ASME
07/23/2012 00:00:00
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6.12 Metal foams

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Metal foams have also been proven to be a viable option in enhancing thermal conductivity of PCMs. High porosity, good thermophysical properties and mechanical strength are salient features of metal foams. ***Examples of applications:*** * The results revealed that the addition of metallic foam improves the heat transfer between the wall of the pipe and the fluid. ERG aluminum foam was the metal foam used in this analysis with a permeability ranging from 10 ppi to 40 ppi. This heat enhancement further improved by adding nanoparticles to the fluid. The heat storage capability of the proposed fluid also increased with the addition of microencapsulated phase change material (MEPCM) particles. The results revealed that 20% MEPCM and 3% nanoparticles in water is an ideal balance for heat storage and enhancement, with a 6.7% improvement in the case of water flowing in a porous pipe. ***Applications:*** * Electronics/Battery storage * Heat exchangers

6.12.1 Metal foams
Analytical considerations of thermal storage and interface evolution of a PCM with/without porous media
Purpose Phase change energy storage is an important solution for overcoming human energy crisis. This study aims to present an evaluation for the thermal performances of a phase change material (PCM) and a PCM–metal foam composite. Effects of pore size, pore density, thermal conductivity of solid structure and mushy region on the thermal storage process are examined. Design/methodology/approach In this paper, temperature, flow field and solid–liquid interface of a PCM with or without porous media were theoretically assessed. The influences of basic parameters on the melting process were analyzed. A PCM thermal storage device with a metal foam composite is designed and a thermodynamic analysis for it is conducted. The optimal PCM temperature and the optimal HTF temperature in the metal foam-enhanced thermal storage device are derived. Findings The results show that the solid–liquid interface of pure PCM is a line area and that of the mixture PCM is a mushy area. The natural convection in the melting liquid is intensive for a PCM without porous medium. The porous medium weakens the natural convection and makes the temperature field, flow field and solid–liquid interface distribution more homogeneous. The metal foam can greatly improve the heat storage rate of a PCM. Originality/value Thermal storage rate of a PCM is compared with that of a PCM–metal foam composite. A thermal analysis is performed on the multi-layered parallel-plate thermal storage device with a PCM embedded in a highly conductive porous medium, and an optimal melting temperature is obtained with the exergy optimization. The heat transfer enhancement with metal foams proved to be necessary for the thermal storage application.
06/20/2019 00:00:00
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6.12.2 Metal foams
Charging nanoparticle enhanced bio-based PCM in open cell metallic foams: An experimental investigation
Abstract In this paper, an experimental investigation is carried out to examine the melting process of nanoparticle enhanced phase change material (i.e., nano-PCM) inside a metal foam enclosure under constant heat flux boundary condition. Visualization experiments were carried out using a bio-based nano-PCM (i.e., copper oxide (CuO) nanoparticles dispersed in the bio-based coconut oil PCM) inside an open-cell metal foam. Rectangular blocks, made from aluminium metal foam of pore density of 5 PPI and porosities of 88%, 92%, and 96%, were considered. An experimental setup was constructed to track the evolution of the melting process and observe the transient variation in temperature. Temperatures were measured at selected locations inside the nano-PCM filled metal foam. Melt fraction was calculated by means of image analysis. Experimentally obtained images corresponding to the melting process of PCM, nano-PCM, PCM in metal foam, and nano-PCM in metal foam are presented for selected times and applied wall heat fluxes. Corresponding melt fractions and energy storage rates are calculated and presented as well. The results showed that utilizing both nanoparticles and metal foam increase the melting and energy storage rates. The results further show uniform melting for low porosity (88%) porous medium as heat is transferred primarily by conduction. For high porosity (96%) porous medium, non-uniform melting, e.g., more melting at the upper part compared to the lower part is observed as heat is transferred by convection at the upper part and by conduction at the lower part. Outcome of the current research can potentially be applied to latent heat thermal energy storage systems, hybrid-electric vehicles’ rechargeable prismatic-battery thermal management systems, and electronic cooling systems in remote locations. The melting process is enhanced by 1.2% when nanoparticles were added to the PCM; however, higher enhancement was observed, i. e. 41.2%, when the metal foam was embedded in the pure PCM at 1814 W/m 2 and 2160 s. The energy stored rate accelerated by utilizing the metal foam in comparison with the pure PCM and the nano-PCM, i. e. 2.61% by adding nanoparticles and 28.81% by utilizing the metal foam at 2835 W/m 2 and 2280 s.
02/01/2019 00:00:00
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6.12.3 Metal foams
Investigation of enclosure aspect ratio effects on melting heat transfer characteristics of metal foam/phase change material composites
Purpose The purpose of this paper is to study thermal performance of metal foam/phase change materials composite under the influence of the enclosure aspect ratios (ratio of enclosure height: length). In this study, a compound metal foam/phase change material (PCM), which has been proved to be one of the most promising approaches for thermal conductivity promotion on PCMs, was used. Design/methodology/approach The PCM is considered initially at its melting temperature. The enclosure for all the cases has a constant volume with various aspect ratios. The left side of the enclosure is suddenly exposed to a thermal source having a constant heat flux, while the other three surfaces are kept thermally insulated. A two-dimensional numerical model considering the non-equilibrium thermal factor, non-Darcy effect and local natural convection was proposed. The coupling between velocity and pressure is solved using the SIMPLEC, and the Rhie and Chow interpolation is used to avoid the checker-board solutions for the pressure. Findings The effects of foam porosity and aspect ratio of the enclosure on the PCM’s melting time were investigated. The results indicated that enclosure aspect ratio plays a fundamental role in phase change of copper foam/PCM composites. For higher porosities, enclosures with bigger aspect ratios proved to led to optimal melting time. Besides, the best enclosure aspect ratio and foam porosity for a fixed-volume enclosure to have the shortest melting time are 2.1 and 91.66 per cent, respectively. However, for a specific amount of PCM inside a variable volume enclosure, the optimal melting time was for foam with e = 95 per cent. The achieved results prove the great importance of selection of aspect ratio to benefit both conduction and convection heat transfer simultaneously. Originality/value The area of energy storage systems is original.
06/28/2019 00:00:00
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6.12.4 Metal foams
Melting and solidification of PCM embedded in porous metal foam in horizontal multi-tube heat storage system
Abstract In this paper, melting and solidification processes of phase change material embedded in metallic porous foam in a multi-tube heat exchanger are investigated numerically under local non-equilibrium thermal condition. RT 35 is used as phase change material in middle shell of 3D multi-tube heat exchanger. Also, water flows across inner tube/tubes and outer tube as a heat transfer fluid (HTF). The effects of number of inner tubes, their arrangement as well as porosity of metallic foam on thermal characteristics of heat storage unit are studied. Results show that increasing number of inner tubes and adding metallic foam enhance melting and solidification rates significantly. A composite of phase change material/metallic foam with porosity of e = 0.7 engenders shorter melting and solidification time comparing to pure PCM. Arrangement of inner tubes has no effect on melting rate of metal foam/PCM composite. By inserting metallic foam with porosities e = 0.9 and e = 0.7 , melting time is decreased by 14% and 55%, respectively. Highest melting rate is for case with four inner tubes for all porosities of metallic foam. Regarding solidification process in pure PCM, case with four tubes shows shorter solidification time. Also, highest solidification rate amid composites of phase change material/metallic foam is seen for case with three tubes. Consequently, inserting metallic foam is more efficient in solidification process rather than the melting one. Moreover, increasing number of inner tubes has more influence on phase change rates in metal foam/PCM composites compared to pure PCM.
09/01/2018 00:00:00
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6.12.5 Metal foams
Numerical study on latent thermal energy storage systems with aluminum foam in local thermal equilibrium
Abstract The paper analyzes the behavior of a Latent Heat Thermal Energy Storage system (LHTES) with a Phase Change Material (PCM), with and without aluminum foam. A numerical investigation in a two-dimensional domain is accomplished to investigate on the system thermal evolution. The enthalpy-porosity method is used to describe the PCM melting. The open-celled aluminum foam is described as a porous medium by means of the Darcy-Forchheimer law. A hollow cylinder represents the considered thermal energy storage and it consists of the enclosure between two concentric shell tubes. The external surface of the internal tube is assigned temperature with a value greater than the melting PCM temperature, while the other surfaces are adiabatic. Local thermal equilibrium (LTE) is numerically adopted for modelling the heat transfer between the PCM and the solid matrix in aluminum foam. In the case with metal foam, simulations for different porosities are performed. A comparison in term of liquid fraction, average temperature of the system, temperature fields, stream function and a performance parameter are made between the clean case and porous assisted case for the different porosities. A scale analysis is developed for evaluating the time and the melting zone in different regimes (i.e. conduction, mixed conduction-convective and convective) during the melting processes of the PCM in porous media. Numerical simulation shows that aluminum foam increases overall heat transfer by a magnitude of two, with respect to the clean case.
08/01/2019 00:00:00
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6.12.6 Metal foams
Role of metallic foam in heat storage in the presence of nanofluid and microencapsulated phase change material
Abstract The focus of this paper is the use of a ternary fluid containing Al 2 O 3 nanoparticles and the microencapsulated phase change material MEPCM. Different heat flux intensities were applied in the outside wall of a porous pipe with fluid entering at different flow rates. The results revealed that the addition of metallic foam improves the heat transfer between the wall of the pipe and the fluid. ERG aluminum foam was the metal foam used in this analysis with a permeability ranging from 10 ppi to 40 ppi. This heat enhancement further improved by adding nanoparticles to the fluid. The heat storage capability of the proposed fluid also increased with the addition of microencapsulated phase change material (MEPCM) particles. The results revealed that 20% MEPCM and 3% nanoparticles in water is an ideal balance for heat storage and enhancement, with a 6.7% improvement in the case of water flowing in a porous pipe.
09/01/2018 00:00:00
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6.12.7 Metal foams
Thermal cooling behaviors of lithium-ion batteries by metal foam with phase change materials
Abstract Lithium ion (Li-ion) batteries are an integral part of electric vehicles and hybrid electric vehicles or smartphones because of their high energy and power density. These batteries suffer from a high temperature rise and generate excessive heat during operation. An improvement technique, passive thermal management (e.g. a phase change material), has become an attractive approach in recent years as it is highly efficient, compact and lightweight. Phase Change Materials (PCMs) store thermal heat in the form of sensible and principally latent heat. PCM changes state from solid to liquid or liquid to gas or vice versa at almost constant temperature during latent heat storage. Metal foams have also been proven to be a viable option in enhancing thermal conductivity of PCMs. High porosity, good thermophysical properties and mechanical strength are salient features of metal foams. In this paper, a simple rectangular electronics passive cooling device was implemented for Li-Ion Battery. A PCM material with metal foam was numerically investigated. Numerical simulations were carried out using the Ansys-Fluent code. Results in terms temperatures, melting time and max reached temperature were reported.
08/01/2018 00:00:00
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6.12.8 Metal foams
Thermal transport augmentation in latent heat thermal energy storage system by partially filled metal foam: A novel configuration
Abstract Thermal transport augmentation in latent heat thermal energy storage (LHTES) system by local installation of metal foam-phase change material (PCM) composite is presented in the current work. The study highlights an optimal concentration and position of metal foam-PCM composite (MFPC) to elevate thermal performance without altering an overall melting time. Thus, a novel configuration MFPC is proposed according to the optimum thermal conductivity enhancer (TCE) density, a criterion defined based on the temporal variation of local temperature gradient during the melting process. The fundamental principle of the criterion is positioning the metal foam only at the maximum thermal potential region for the effective utilization efficiency of the metal foam. A numerical code based on a local thermal non-equilibrium coupled enthalpy porosity approach is developed and validated. The numerical results showed that the proposed configuration with the provision of MFPC at a high thermal potential region alleviates local conductive transport with enhancement in the overall melting rate. It is seen that the withdrawal of metal mass at low thermal potential region encompasses the beneficial influence of natural convective transport, which is observed to be impeded in the previous configuration. The total melting time is observed to be equal for the proposed configuration when compared to the LHTES with the full volume of metal foam. The elimination of metal mass can increase the mass of PCM and thermal energy storage capacity. Additionally, it can assist to reduce weight and economy of the LHTES system.
04/01/2019 00:00:00
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6.13 Fine powdered composite for latent heat storage

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Sorption heat storage implies the use of physical or chemical bonds to store energy. The principle of sorption occurs during a reaction, and in order to take place, at least two components are needed: a sorbent, which is typically a liquid or solid, and a sorbate, which is typically a vapor. During the charging process, an endothermic reaction occurs, and the sorbent and sorbate are separated. The two components can then be stored separately, ideally without energy losses. During the discharging process, sorbent and sorbate react producing an exothermic reaction that releases heat. The main advantages of sorption heat storage are higher energy density and negligible heat losses compared to a conventional thermal storage based on sensible heat. A conventional water storage needs to be approximately five to ten times larger than a sorption heat storage system for storing the same energy. In this specific case, the system uses the reaction energy created when salts are hydrated or dehydrated. It can work by storing heat in a container containing 50% sodium hydroxide (NaOH) solution. Heat (e.g. from using a solar collector) is stored by evaporating the water in an endothermic reaction. When water is added again, heat is released in an exothermic reaction at 50 °C (120 °F). Generally, current systems operate at 60% efficiency. The system is especially advantageous for seasonal thermal energy storage, because the dried salt can be stored at room temperature for prolonged times, without energy loss. The containers with the dehydrated salt can even be transported to a different location. The system has a higher energy density than heat stored in water and the capacity of the system can be designed to store energy from a few months to years.

6.13.1 Fine powdered composite for latent heat storage
Energy density and storage capacity cost comparison of conceptual solid and liquid sorption seasonal heat storage systems for low-temperature space heating
Sorption heat storage can potentially store thermal energy for long time periods with a higher energy density compared to conventional storage technologies. A performance comparison in terms of energy density and storage capacity costs of different sorption system concepts used for seasonal heat storage is carried out. The reference scenario for the analysis consisted of satisfying the yearly heating demand of a passive house. Three salt hydrates (MgCl2, Na2S, and SrBr2), one adsorbent (zeolite 13X) and one ideal composite based on CaCl2, are used as active materials in solid sorption systems. One liquid sorption system based on NaOH is also considered in this analysis. The focus is on open solid sorption systems, which are compared with closed sorption systems and with the liquid sorption system. The main results show that, for the assumed reactor layouts, the closed solid sorption systems are generally more expensive compared to open systems. The use of the ideal composite represented a good compromise between energy density and storage capacity costs, assuming a sufficient hydrothermal stability. The ideal liquid system resulted more affordable in terms of reactor and active material costs but less compact compared to the systems based on the pure adsorbent and certain salt hydrates. Among the main conclusions, this analysis shows that the costs for the investigated ideal systems based on sorption reactions, even considering only the active material and the reactor material costs, are relatively high compared to the acceptable storage capacity costs defined for different users. However, acceptable storage capacity costs reflect the present market condition, and they can sensibly increase or decrease in a relatively short period due to for e.g. the variation of fossil fuels prices. Therefore, in the upcoming future, systems like the ones investigated in this work can become more competitive in the energy sector.
09/01/2017 00:00:00
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6.13.2 Fine powdered composite for latent heat storage
Improvement in flowability of thermo-chemical storage material by using nanostructured additives
Thermal energy storage is an advancing technology for storing energy that encourages clean energy systems without adversely affecting the environment. This technology allows us to use energy at different times by storing it temporarily. For example in a non-conventional energy source like solar thermal power plant, all its energy is produced during broad day light. The excess energy produced during a sunny day is usually stored in the thermal storage materials, which can later be used in the night to generate electricity. One such advantageous way of storing energy is through thermo-chemical storage. In a space craving society, high storage capability makes it an efficient way to store energy. However at present thermo-chemical storage is in its elementary stage, where in its limited to only one pilot scale system. Considering the thermodynamics and kinetics it has been shown that CaO/Ca(OH)2 reaction system is a potential gas/solid thermochemical heat storage system. However the behavior in a lab sized non-moving bed reactor was mainly dominated by heat and mass transfer limitations arising due to small particle size and changes in bulk properties. This was overcome to a certain level using a moving bed reactor but due to the change in the reactor type the flowability factor dominated adversely. Nevertheless during the recent studies at DLR it was found out that small amount of industrial grade SiO2 (Aerosil®) nanoparticles would enhance the flowability of Ca(OH)2 in a considerable way. But in contrast it effects the heat development leading to low thermal efficiency due to the formation of inert side products. In this study it is found out that small amount of nanostructured Al2O3 (Aeroxide®) not only plays a significant role in stabilizing cyclability and bulk properties but also contributes to the overall heat development.
06/01/2015 00:00:00
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6.13.3 Fine powdered composite for latent heat storage
Solid–gas thermochemical sorption thermal battery for solar cooling and heating energy storage and heat transformer
Thermal energy storage plays a vital role in the sustainable utilization of solar energy for heating and cooling applications due to its inherent instability and discontinuity. An advanced high-performance solid–gas thermochemical sorption thermal battery is developed for solar cooling and heating energy storage and heat transformer. Solar thermal energy is stored in the form of bond energy during the charging phase and the stored energy is released in the form of heat and cold energy during the discharging phase based on the energy conversion between thermal energy and bond energy of sorption potential during the solid–gas sorption process of working pair. The heat and cold energy storage densities are as high as 1300–1600 kJ/kg and 640–720 kJ/kg respectively when the sorption thermal battery using working pair of SrCl2–NH3 works as short-term and long-term seasonal energy storage. Moreover, the working temperature of stored energy can be effectively upgraded by using the sorption thermal battery. It appears that the proposed sorption thermal battery is an effective method for the short-term and long-term storage of solar thermal energy, and it has distinct advantages of combined cold and heat storage, high energy density, integrated energy storage and energy upgrade in comparison with conventional energy storage methods.
05/01/2015 00:00:00
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6.13.4 Fine powdered composite for latent heat storage
Thermophysical characterization and thermal cycling stability of two TCM: CaCl2 and zeolite
At this moment, the global energy consumption in buildings is around 40% of the total energy consumption in developed countries. Thermal energy storage (TES) is presented as one way to address this energy-related problem proposing an alternative to reduce the gap between energy supply and energy demand. One way to store energy is using thermochemical materials (TCM). These types of materials allow accumulating energy through a chemical process at low temperature, almost without heat losses. In addition, it is a stable way to perform the heat storage and TCM can be implemented for seasonal storage or/and long term storage. This study compares the cyclability, from the thermophysical point of view, CaCl2 which follows a chemical reaction and zeolite which follows a sorption process to be used as TCM for seasonal/long term storage. The main results show that the chemical reaction TCM is more energy-efficient than the sorption TCM. The CaCl2 calculated energy density is 1.47GJ/m3, being the best option to be considered to be used as TCM, even though the dehydration process of the zeolite is simpler and it occurs at higher temperatures its calculated energy density is only 0.2GJ/m3.
01/01/2015 00:00:00
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6.13.5 Fine powdered composite for latent heat storage
Trouton's rule for vapor sorption in solids
Hygroscopic salts exhibiting fast and reversible hydration are promising systems for seasonal heat storage, providing the possibility of storing excess solar energy from the warm season for later use during the cold season. For heat storage, the salt is dehydrated with the available heat, and for heat recovery, the salt is rehydrated. There are many salt hydration transitions and for selecting the most suited ones with respect to the envisaged use cases, temperatures of dehydration and rehydration are needed, as well as the heat storage density. Estimation of these properties requires entropy and enthalpy changes of the transitions. Collections of hydration entropies and enthalpies have been published, but not all data seems reliable for various reasons, and it is often hard to access original sources and experimental conditions. For the necessary data validation, we propose the use of Trouton’s rule, known to hold for the evaporation of classes of fluids. Besides data validation, Trouton’s rule is useful for predicting heat storage densities and vapor pressures when only the transition enthalpy is known. We discuss the validity of Trouton’s rule for salt hydration and ammoniation transitions by theoretical and experimental evidence on the available extensive data collections.
04/20/2018 00:00:00
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7. Thermochemical heat storage (THS)

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THS systems can utilise both sorption and chemical reactions to generate heat and in order to achieve efficient and economically acceptable systems, the appropriate reversible reactions (suitable to the user demand needs) need to be identified. In general THS have specific energy within the range of 120-250 kWh/t and an energy capacity of 120-250 kWh/m³. This is the highest compared to the other methods. The efficiency of this system can be very high in the range of 75-95% efficiency (potential), however, this has yet to be proven in practice. The storage period for these systems is about hour-week based. And the cost of these systems is 8-100 €/kWh which is relatively the most expensive on large scale. The price can go down significantly with time when concepts become more robust. General advantages of chemical heat storage: * High energy density * Compact in size * Almost no losses in energy possible (high efficiency) * Potential of being non-toxic General disadvantages of chemical heat storage: * Instability of materials * Cycling problems * Complex systems * High materials cost


7.1 Hydroxides (M(OH)₂)

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The dehydration reaction of metal hydroxides can lead to high heat storage efficiency and places these chemicals as candidates for thermochemical heat storage. Ca(OH)₂/CaO system shows the highest enthalpy of reaction, followed by Mg(OH)₂/MgO. The reversible reaction of dehydration/ rehydration of Ca(OH)₂ has attracted attention, because it is a cheap material and it features a high enthalpy of reaction, and therefore it has already been studied for potential application inenergy storage Based on: Ca, Mg, Be, Mn, Sr, Ba, Ni, Zn, Cd ***Applications:*** * Domestic seasonal energy storage * Given the proven interest of hydroxides for low temperature TES, their study needs to be extended to appraise their applicability to high temperature CSP plants.

7.1.1 Hydroxides (M(OH)₂)
Behavior of Ca(OH)2/CaO pellet under dehydration and hydration
With construction of a thermochemical energy conversion prototype system to store solar heat, thermal dissociation of pellets of Ca(OH)2 and hydration of CaO have been investigated in some detail for its application to the system. The inorganic substance is very attractive as a material for long term heat storage, but molar density changes associated with the reaction are fairly large. Therefore, this factor has been taken into account in the kinetic equation. The importance of additives and pellet size has been discussed considering reactivity and strength of pellets. An analysis has been attempted when chemical reaction is important. The deformation of pellets was observed during hydration.
10/01/1994 00:00:00
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7.1.2 Hydroxides (M(OH)₂)
CaO/Ca(OH)2 thermochemical heat storage of carbide slag from calcium looping cycles for CO2 capture
Abstract Carbide slag is an industrial waste generated from ethylene gas production in chlor-alkali plants. Here, a novel system coupling calcium looping and CaO/Ca(OH) 2 thermochemical heat storage using carbide slag were proposed to simultaneously capture CO 2 and store heat. For CaO/Ca(OH) 2 thermochemical heat storage, the hydration/dehydration performance of original carbide slag and carbide slag that experienced calcium looping cycles for CO 2 capture was investigated. The performances of the two types of carbide slag with and without chlorine were compared. The dehydration conversions of carbide slag improved with the increase of dehydration temperature. The chlorine content has no apparent effect on the hydration/dehydration performance of original carbide slag. However, for CO 2 capture, carbide slag with high chlorine content shows lower carbonation conversion than that of carbide slag without chlorine. The hydration/dehydration conversions of carbide slag that experienced CO 2 capture cycles are lower than those of original carbide slag. For carbide slag with chlorine, the hydration conversion can be improved by more than one CO 2 capture cycle. Therefore, carbide slag that experienced various CO 2 capture cycles is still suitable to be used in CaO/Ca(OH) 2 thermochemical heat storage although calcium looping has an adverse effect on the hydration/dehydration performance of carbide slag.
10/01/2018 00:00:00
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7.1.3 Hydroxides (M(OH)₂)
Experience on the Development of a Thermo-chemical Storage System Based on Aqueous Sodium Hydroxide☆
Abstract Closed sorption heat storage opens up a way to achieve seasonal thermal storage without loss during storage. Thermal energy is not stored as sensible heat or latent heat, but by the separation of substances. In this manner it is possible to store heat, or better said, the potential to regain heat. Such a system functioning as an absorption heat pump with intermediate storage is well suited for long term thermal energy storage. Nevertheless, the conversion losses in both the regenerating and heating process make it inferior to sensible thermal storage for short storage cycles. For this reason a hybrid system including a water tank as sensible thermal storage to cover the thermal demands of several days, and a closed sorption heat storage to cover longer periods of insufficient solar thermal input is proposed. The storage system energy density is directly proportional to the sorbate mass difference between regenerated and diluted sorbent. In order to reach high utilization, a large dilution in the sorbent must be reached during heating mode. Thus, the operating temperature parameters must be adjusted and regulated accordingly. In the scope of the EU funded project COMTES, a prototype system based on the working pair sodium hydroxide and water is under construction. The system is dimensioned to cover space heating as well as domestic hot water in a single family house in Zurich, built to passive energy standards. The prototype is starting operation in spring 2014 whereby the system is regenerated to be ready to cover the heating demands the following winter.
01/01/2014 00:00:00
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7.1.4 Hydroxides (M(OH)₂)
Feasibility analysis of a novel solid-state H2 storage reactor concept based on thermochemical heat storage: MgH2 and Mg(OH)2 as reference materials
This paper discusses the feasibility of a novel adiabatic magnesium hydride (MgH2) reactor concept based on thermochemical heat storage. In such a concept, the heat of reaction released during the absorption of hydrogen is stored by a thermochemical material in order to be reused in a subsequent desorption stage. Magnesium hydroxide (Mg(OH)2) has been selected as the suitable material for integration into the MgH2 storage system due to its thermodynamic properties. An analytical formulation of hydrogen absorption time is used to determine the range of the geometrical characteristics of the two storage media, their properties and their operating conditions. The advantage of the proposed new concept is the possibility to reduce the mass of the heat storage media by a factor of 4 compared to phase change material, improving then the gravimetric system capacity as well as its total cost. The second advantage is an improved flexibility of the operating pressure conditions for MgH2 absorption reaction and Mg(OH)2 dehydration reaction that enables shorter hydrogen absorption times by ensuring larger temperature gradients between the two storage media.
12/01/2016 00:00:00
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7.1.5 Hydroxides (M(OH)₂)
High Temperature Thermochemical Energy Storage Using Packed Beds
Thermal energy storage units are vital for development of the efficient solar power generation systems due to fluctuating nature of daily and seasonal solar radiations. Two available efficient and practical options to store and release solar energy at high temperatures are latent heat storage and thermochemical storage. Latent heat storage can operate only at single phase change temperature. This problem can be avoided by some of the thermochemical storage systems in which solar energy can be stored and released over a range of high temperature by endothermic and exothermic reactions. One such reaction system is reversible reaction involving dehydration of Ca(OH)2 and hydration of CaO. This system is considered in the present study to model a circular fixed bed reactor for storage and release of heat at high temperatures. Air is used as heat transfer fluid (HTF) flowing in an annular shell outside the bed for charging and discharging the bed. The bed is filled with CaO/Ca(OH)2 powders with particles diameter of the order 5μm. Three dimensional transient model has been developed and simulations are performed using finite elements based COMSOL Multiphysics. Conservation of mass and energy equations, coupled with reaction kinetics equations, are solved in the three dimensional porous bed and the heat transfer fluid channel. Parametric study is performed by varying HTF parameters, bed dimensions and process conditions. The results are verified through a qualitative comparison with experimental and simulation results in the literature for similar geometric configurations.Copyright © 2016 by ASME
11/11/2016 00:00:00
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7.1.6 Hydroxides (M(OH)₂)
High-temperature high-density heat storage using Ca(OH){sub 2}/CaO thermochemical reaction
The applicability of Ca(OH ){sub 2}/CaO thermochemical reaction for high temperature level heat utilization and for storing heat converted from night-time electricity was studied. The operating temperature level and heat releasing/storing rate were investigated by means of lab-scale heat storage units and the results were evaluated in terms of theoretical values. It was found that the temperature of the CaO reactant bed during the heat-releasing step carried out under 500k Pa water vapor is upgraded from 773 K to 873 K. Complete regeneration was obtained under 670 K and 2-3 kPa. Another practical feature of this type of thermal energy storage system was proven by using an adiabatic reactor incorporated with a fin-type heat exchanger where the produced heat of hydration was recovered by raising the temperature of water from 300 K to 343 K for domestic use. The amount of the heat recovered by this storage unit was about 4 times higher than that will be recovered if the energy storage was carried out by sensible heat of water in the same volume. 4 refs., 11 figs.
12/31/1996 00:00:00
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7.1.7 Hydroxides (M(OH)₂)
Screening of thermochemical systems based on solid-gas reversible reactions for high temperature solar thermal energy storage
A viable way to manage the inherently intermittent availability of solar energy in concentrated solar power plants is to store solar energy during on-sun hours to be able to use it later during off-sun hours, enabling on-demand electricity delivery. Thermochemical heat storage systems present some noteworthy advantages when compared with latent and sensible heat storage, namely (i) high energy storage density because the storage capacity by unit of mass or volume corresponding to the reaction enthalpy is generally high, (ii) heat storage at room temperature and long term energy storage because the products can be cooled and stored at room temperature without energy losses as heat can be stored indefinitely in chemical bonds, (iii) facility of transport because solid materials can be transferred over long distances, (iv) constant restitution temperature providing constant heat source because exothermic reactions are carried out at sufficiently high temperatures to generate electricity in constant conditions and therefore to produce a constant power. This paper presents an overview of the different potential thermochemical systems based on reversible solid-gas reactions operating at high temperatures and a screening of suitable materials that are interesting candidates in the 400–1200°C range for thermochemical heat storage in concentrated solar power systems. The most promising materials belonging to the metal oxides, hydroxides, and carbonates solid-gas systems are selected for experimental validation and further investigations.
10/01/2016 00:00:00
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7.2 Metal Carbonates (MCO₃)

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Metal carbonates have mainly been proposed and studied as sorbent materials in the context of CO₂ capture. The capture and storage of carbon dioxide has become of prime interest in order to reduce the concentration of greenhouse gases in the atmosphere and as such, literature data on the thermal behavior of sorbents (especially calcium oxide-based sorbents) during carbonation/calcination looping cycles is abundant. Metal carbonates are also potential candidates for thermochemical heat storage with some of them showing remarkable high reaction enthalpy and energy storage density. Based on: Ca, Sr, Mg, Ba, Cd, Zn, Pb ***Applications:*** * Metal carbonates show potential to store and release heat via reversible reactions and they are thus considered to be worthy for heat storage applications * CO₂ sorption * The potential of theSrCO₃/SrO couple for thermochemical energy storage application. The sintering of SrOover several carbonation steps was addressed by using 40 wt. % of SrO supported on yttria-stabilized zirconia. This way, the material remained stable over 15 cycles, with energy storage density stabilized at approximately 1400760 MJ/m³. Degradation of the capacity of the material is however noticed after about 45 cycles.

7.2.1 Metal Carbonates (MCO₃)
Application of lithium orthosilicate for high-temperature thermochemical energy storage
A lithium orthosilicate/carbon dioxide (Li4SiO4/CO2) reaction system is proposed for use in thermochemical energy storage (TcES) and chemical heat pump (CHP) systems at around 700°C. Carbonation of Li4SiO4 exothermically produces lithium carbonate (Li2CO3) and lithium metasilicate (Li2SiO3). Decarbonation of these products is used for heat storage, and carbonation is used for heat output in a TcES system. A Li4SiO4 sample around 20μm in diameter was prepared from Li2CO3 and SiO2 using a solid-state reaction method. To determine the reactivity of the sample, Li4SiO4 carbonation and decarbonation experiments were conducted under CO2 at several pressures in a closed reactor using thermogravimetric analysis. The Li4SiO4 sample’s carbonation and decarbonation performance was sufficient for use as a TcES material at around 700°C. In addition, both reaction temperatures of Li4SiO4 varied with the CO2 pressure. The durability under repeated Li4SiO4 carbonation and decarbonation was tested using temperature swing and pressure swing methods. Both methods showed that the Li4SiO4 sample has sufficient durability. These results indicate that the temperature for heat storage and heat output by carbonation and decarbonation, respectively, could be controlled by controlling the CO2 pressure. Li4SiO4/CO2 can be used not only for TcES but also in CHPs. The volumetric and gravimetric thermal energy densities of Li4SiO4 for TcES were found to be 750kJL−1 and 780kJkg−1, where the porosity of Li4SiO4 was assumed to be 59%. When the reaction system was used as a CHP, and heat stored at 650°C was warmed and output at 700°C, 14% of the heat supplied by carbonation was needed for self-heating of the material from 650 to 700°C, and the volumetric and gravimetric thermal energy densities for heat output were calculated as 650kJL−1 and 670kJkg−1, respectively.
05/01/2017 00:00:00
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7.2.2 Metal Carbonates (MCO₃)
Evaluation and performances comparison of calcium, strontium and barium carbonates during calcination/carbonation reactions for solar thermochemical energy storage
Abstract The efficiency and economic competitiveness of thermal storage for concentrating solar power plant can be improved by increasing the operating temperature (above 600 °C). Thermochemical energy storage is an attractive way of efficiently storing high-temperature solar heat, in the form of chemical bonds as a stable and safe solid material, when compared with existing sensible and latent heat storage materials. Among the most interesting materials, BaCO 3 , CaCO 3 and SrCO 3 show high storage temperatures (typically above 800 °C), energy storage densities, and charging and discharging rates. Heat charge corresponds to the calcination (decarbonation) reaction of the carbonates (endothermal step) and heat discharge corresponds to the reverse carbonation of the oxides (exothermal step). A comparative thermodynamic and kinetic study of calcination and carbonation reactions involving commercial and synthesized CaCO 3 , SrCO 3 and BaCO 3 powders was performed for application in thermochemical energy storage. An experimental study based on thermogravimetric analysis (TGA) and differential scanning calorimetry (DSC) was conducted to study the decomposition and carbonation reactions and to determine the enthalpy of reaction for each metal carbonate. While complete calcination was achieved regardless of the metal carbonate involved, partial carbonation was observed with loss in CO 2 capture capacity during cycling. The effect of the addition of a promoting agent such as magnesium oxide on thermal stability for improving chemical and structural cyclability of these three candidate carbonates was also investigated. Beneficial effect of MgO addition was demonstrated and noticeable performance stability was obtained in the case of SrCO 3 /SrO during successive energy storage cycles.
10/01/2017 00:00:00
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7.2.3 Metal Carbonates (MCO₃)
Hydration of Magnesium Carbonate in a Thermal Energy Storage Process and Its Heating Application Design
First ideas of applications design using magnesium (hydro) carbonates mixed with silica gel for day/night and seasonal thermal energy storage are presented. The application implies using solar (or another) heat source for heating up the thermal energy storage (dehydration) unit during daytime or summertime, of which energy can be discharged (hydration) during night-time or winter. The applications can be used in small houses or bigger buildings. Experimental data are presented, determining and analysing kinetics and operating temperatures for the applications. In this paper the focus is on the hydration part of the process, which is the more challenging part, considering conversion and kinetics. Various operating temperatures for both the reactor and the water (storage) tank are tested and the favourable temperatures are presented and discussed. Applications both using ground heat for water vapour generation and using water vapour from indoor air are presented. The thermal energy storage system with mixed nesquehonite (NQ) and silica gel (SG) can use both low (25–50%) and high (75%) relative humidity (RH) air for hydration. The hydration at 40% RH gives a thermal storage capacity of 0.32 MJ/kg while 75% RH gives a capacity of 0.68 MJ/kg.
01/11/2018 00:00:00
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7.2.4 Metal Carbonates (MCO₃)
Screening of thermochemical systems based on solid-gas reversible reactions for high temperature solar thermal energy storage
A viable way to manage the inherently intermittent availability of solar energy in concentrated solar power plants is to store solar energy during on-sun hours to be able to use it later during off-sun hours, enabling on-demand electricity delivery. Thermochemical heat storage systems present some noteworthy advantages when compared with latent and sensible heat storage, namely (i) high energy storage density because the storage capacity by unit of mass or volume corresponding to the reaction enthalpy is generally high, (ii) heat storage at room temperature and long term energy storage because the products can be cooled and stored at room temperature without energy losses as heat can be stored indefinitely in chemical bonds, (iii) facility of transport because solid materials can be transferred over long distances, (iv) constant restitution temperature providing constant heat source because exothermic reactions are carried out at sufficiently high temperatures to generate electricity in constant conditions and therefore to produce a constant power. This paper presents an overview of the different potential thermochemical systems based on reversible solid-gas reactions operating at high temperatures and a screening of suitable materials that are interesting candidates in the 400–1200°C range for thermochemical heat storage in concentrated solar power systems. The most promising materials belonging to the metal oxides, hydroxides, and carbonates solid-gas systems are selected for experimental validation and further investigations.
10/01/2016 00:00:00
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7.2.5 Metal Carbonates (MCO₃)
Thermal storage of (solar) energy by sorption of water in magnesium (hydro) carbonates
In this paper the thermodynamic properties and the chemical reaction kinetics of the reversible reactions where sorption of water in magnesium hydro carbonates are analysed for thermal energy storage (TES). Depending on the conditions mainly nesquehonite, lansfordite and hydromagnesite may be formed from magnesite, all with a certain heat effect. Magnesite and water vapour can form nesquehonite or lansfordite via reaction (R1) and (R2): MgCO3 + 3H2O(g) ↔ MgCO3∙3H2O ΔH = -1.83 MJ/kg MgCO3, T=298K (R1) MgCO3 + 5H2O(g) ↔MgCO3∙5H2O ΔH = -2.54 MJ/kg MgCO3, T=298K (R2) Compared to other chemical sorption compounds, its advantages are low operating temperatures while they can act as a fire retardant. Experimental data is presented on the reactivity of the dehydration at various temperatures. The rate of dehydration of the nesquehonite is sufficient at low temperatures such as 50 °C and the reaction is about 90 % completed after 120 minutes. Magnesite reaches partial re-hydration to about 37% conversion after 24 hours. For better contact between reagents, mixtures with silica gel were used. A too large amount of water vapour, causing condensation of the water, appears to make the reactions irreversible. The temperatures of operating the process are presented as well as which compounds give an optimal energy storage.
05/31/2017 00:00:00
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7.2.6 Metal Carbonates (MCO₃)
THERMAL STORAGE OF (SOLAR) ENERGY BY SORPTION OF WATER IN MAGNESIUM (HYDRO) CARBONATES
In this paper the thermodynamic properties and the chemical reaction kinetics of the reversible reactions where sorption of water in magnesium (hydro)carbonates are analysed for thermal energy storage. Depending on the conditions mainly nesquehonite, lansfordite and hydromagnesite may be formed from magnesite, all with a certain heat effect [1]. Magnesite and water vapour can form nesquehonite or lansfordite [2]: MgCO 3 + 3H 2 O(g) = MgCO 3 ∙3H 2 O   ΔH = -1760 kJ/kg MgCO 3 MgCO 3 + 5H 2 O(g) = MgCO 3 ∙5H 2 O  ΔH = -2540 kJ/kg MgCO 3 In a mildly alkaline solution the following reaction can occur producing hydromagnesite: 5MgCO 3 + 2OH - (aq) + 4H 2 O(l/g) = Mg 5 (OH) 2 (CO 3 ) 4 ∙4H 2 O + CO 3 2- (aq) ΔH = -30/-192 kJ/kg MgCO 3 In practice, this would take place in a storage tank located below a house, or possibly in the wall of a house. Technology can be developed for heating a house or other building that uses daytime solar energy to drive the endothermic reactions while during night time the reverse reaction will generate heat for the building. The temperatures of operating the process are presented and which compounds give an optimal energy storage. The temperature levels will be such that integration with district heating systems is possible, perhaps also with more modern district heating operating at relatively low temperatures. The energy storage capacity per tonne of MgCO 3 as hydrated nesquehonite and lansfordite is up to 5 respectively 7 times better than heating up water by 80°C. Experimental data will be presented on the kinetics at various temperatures and relative humidities studying which type of hydrated magnesium carbonate is formed and under which conditions. Repeatability of the reversible reactions is also examined, considering that it should take place at one cycle per day. Different water vapour absorbents as zeolite or silica gel are being tested, removing the moisture produced by the dehydration steps [3]. A too high amount of water vapour, causing condensation of the water, seems to make the reactions irreversible. First results agree with findings by others [4]. References [1]   Zevenhoven, R., Slotte, M., Abacka, J., Highfield, J. 2015. A comparison of CO 2 mineral carbonation processes involving a dry or wet carbonation step. ENERGY - The International Journal (Special edition for ECOS’2015) – submitted (October 2015) [2]   HSC Chemistry version 8.1.1. Reaction equations. 2014. Outokumpu Research. Pori, Finland. [3]   Hongois, S., Kuznik, F., Stevens, P., Roux., J-J. 2011. Development and characterization of a new MgSO 4 -zeolite composite for long-term thermal energy storage. Solar Energy Material & Solar Cells, 85, 1831-1837 [4]   Morgan, B., Wilson, S., Madsen, I., Gozukara., J. 2015. Increased thermal stability of nesquehonite (MgCO 3 *H 2 O) in the presence of humidity and CO 2 : Implications for low-temperature CO 2 storage, International Journal of Greenhouse Gas Control, 39, 366-376
08/25/2016 00:00:00
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7.3 Metal sulfates (MSO₄)

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Metal sulfates have been studied for application as heat storage media for solar energy. Metal sulfates are potential candidates for thermochemical heat storage because they exhibit high reaction enthalpies and can be suitable for operating with concentrated solar energy since their operating temperatures are comprised between roughly 900 °C and 1400 °C . Based on: Mn, Fe, Co, Cu, Ba, Zn, Cd, Ni ***Applications:*** * The potential of using sulfates as thermo-chemical energy storage media. However, the use of sulfates introduces a critical issue of corrosion which has to be taken into account when choosing the materials for the storage system

7.3.1 Metal sulfates (MSO₄)
Material screening for two-step thermochemical splitting of H2S using metal sulfide
Associated with the rise in energy demand is the increase in the amount of H 2 S evolved to the environment. H 2 S is toxic and dangerous to life and the environment, thus, the need to develop efficient and costeffective ways of disposing of the H 2 S gas has become all-important. To this end, a two-step thermochemical H 2 S splitting cycle is proposed in this work which does more than just getting rid of the toxic gas but has the potential to produce valuable H 2 gas as well as store the solar heat energy. Studies have proved that the type of material used, such as metal sulfides, is critical to the efficiency of this thermochemical splitting process. As follows, this study focuses on establishing a criterion to aid in selecting favorable metal sulfides for application and further development in the H 2 S thermochemical decomposition sphere. Using a computational approach, via the HSC Chemistry 8®, evaluations such as the equilibrium yield from the sulfurization and decomposition reaction steps, the temperature required for reaction spontaneity, and the Reversibility Index were determined. Investigations proved that sulfides of Zirconium, Niobium, and Nickel were auspicious candidates for the thermochemical decomposition.
01/01/2019 00:00:00
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7.3.2 Metal sulfates (MSO₄)
Screening of thermochemical systems based on solid-gas reversible reactions for high temperature solar thermal energy storage
A viable way to manage the inherently intermittent availability of solar energy in concentrated solar power plants is to store solar energy during on-sun hours to be able to use it later during off-sun hours, enabling on-demand electricity delivery. Thermochemical heat storage systems present some noteworthy advantages when compared with latent and sensible heat storage, namely (i) high energy storage density because the storage capacity by unit of mass or volume corresponding to the reaction enthalpy is generally high, (ii) heat storage at room temperature and long term energy storage because the products can be cooled and stored at room temperature without energy losses as heat can be stored indefinitely in chemical bonds, (iii) facility of transport because solid materials can be transferred over long distances, (iv) constant restitution temperature providing constant heat source because exothermic reactions are carried out at sufficiently high temperatures to generate electricity in constant conditions and therefore to produce a constant power. This paper presents an overview of the different potential thermochemical systems based on reversible solid-gas reactions operating at high temperatures and a screening of suitable materials that are interesting candidates in the 400–1200°C range for thermochemical heat storage in concentrated solar power systems. The most promising materials belonging to the metal oxides, hydroxides, and carbonates solid-gas systems are selected for experimental validation and further investigations.
10/01/2016 00:00:00
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7.3.3 Metal sulfates (MSO₄)
Thermal energy storage in porous materials with adsorption and desorption of moisture
Abstract Sensible and latent heat that is stored in materials cannot be typically used over long periods, such as seasons, due to heat losses. Storing thermal energy in the form of chemical potential circumvents this issue. We present a numerical model capable of simulating adsorption/desorption based energy release/storage processes for given input material properties, operating conditions and geometric configurations. Since an analysis of flow in porous media can involve a multitude of empirical constants, making the design tool less general, our approach is more fundamental. The model is based on the species transport equation to characterize the adsorption and desorption in a porous solid and is validated against an experimental study. Without requiring microscopic details of pore structure, it provides the spatial and temporal variations in moisture concentration and temperature during the adsorption and desorption processes in the porous material. Through parametric variations of input conditions, the proposed model/tool can be used to identify adsorbent–adsorbate pairs for optimal performance.
02/01/2014 00:00:00
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7.4 Pure metal oxides (MO)

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Various metal oxides have been studied for thermochemical heat storage applications due to their high gravimetric storage density, which is important for lowering the necessary amount of reactant involved in large-scale process. Based on: Rh, V, Ca, Mn, Cu, Li, Fe, Ba, Ng, Cr, Pt, Pb, Sb, U, Mg ***Applications:*** * They possess a wide range of operating temperatures starting from 145°C until up to 1700°C, which can help adapting the process to several kinds of Concentrated Solar Power technologies. * Thermochemical heat storage based on redox reactions usingmetal oxides also presents the advantage of directly using air as heat transferfluid. Without the necessity to store the heat transferfluid, it becomes possible to work with an open loop system, incontrast to metal sulfates or carbonates that require a closed-loop. * Various metal oxides have been studied for thermochemical heat storage applications due to their high gravimetric storage density, which is important for lowering the necessary amount of reactant involved in large-scale process.

7.4.1 Pure metal oxides (MO)
Evaluation of energy density as performance indicator for thermal energy storage at material and system levels
Abstract The increase of the capacity factor of thermal processes which use renewable energies is closely linked to the implementation of thermal energy storage (TES) systems. Currently, TES systems can be classified depending on the technology for storing thermal: sensible heat, latent heat, and sorption and chemical reactions (usually known as thermochemical energy storage). However, there is no standardized procedure for the evaluation of such technologies, and therefore the development of performance indicators which suit the requisites of the final users becomes an important goal. In the present paper, the authors identified the energy density as an important performance indicator for TES, and evaluated it at both material and system levels. This approach is afterwards applied to prototypes covering the three TES technologies: a two-tank molten salts sensible storage system, a shell-and-tube latent heat storage system, and a magnesium oxide and water chemical storage system. The evaluation of the energy density highlighted the difference of its value at the material value, which presents a theoretical maximum, and the results at system level, which considers all the parts required for operating the TES, and thus presents a significantly lower value. Moreover, the proposed approach captured the effect of the complexity and overall size of the system, showing the relevance of this performance indicator for evaluating technologies for applications in which volume is a limiting parameter.
02/01/2019 00:00:00
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7.4.2 Pure metal oxides (MO)
Hybrid Sensible/Thermochemical Storage of Solar Energy in Cascades of Redox-Oxide-Pair-Based Porous Ceramics
The current work is a follow-up of the idea described in previous publications, namely of combining active thermochemical redox oxide pairs like Co3O4/CoO, Mn2O3/Mn3O4 or CuO/Cu2O with porous ceramic structures in order to effectively store solar heat in air-operated Solar Tower Power Plants. In this configuration the storage concept is rendered from “purely” sensible to a “hybrid” sensible/thermochemical one and the current heat storage recuperators to integrated thermochemical reactors/heat exchangers. In addition, the construction modularity of the current state-of-the-art sensible storage systems provides for the implementation of concepts like spatial variation of redox oxide materials chemistry and solid materials porosity along the reactor/heat exchanger, to enhance the utilization of the heat transfer fluid and the storage of its enthalpy. In this perspective the idea of employing cascades of various porous structures, incorporating different redox oxide materials and distributed in a certain rational pattern in space tailored to their thermochemical characteristics and to the local temperature of the heat transfer medium has been set forth and tested.Thermogravimetric analysis (TGA) studies described in previous works have shown that the Co3O4/CoO redox pair with a reduction onset temperature ≈ 885–905°C is capable of stoichiometric, long-term, cyclic reduction-oxidation under a variety of heatup/cooldown rates. Further such studies with the other two powder systems above, described herein, have demonstrated that the Mn3O4/Mn2O3 redox pair is characterized by a large temperature gap between reduction (≈ 950°C) and oxidation (≈ 780–690°C) temperature, whereas the CuO/Cu2O pair cannot work reproducibly and quantitatively since its redox temperature range is narrow and very close to the melting point of Cu2O. Thus, a combination of two such systems, namely Co3O4/CoO and Mn2O3/Mn3O4 has been further explored. Thermal cycling tests with these two powders together under the conditions required for complete oxidation of the less “robust” one, namely Mn3O4/Mn2O3, demonstrated in principle the proof-of-concept of the cascaded configuration, i.e. that both powders can be reduced and oxidized in complementary temperature ranges, extending thus the temperature operation window of the whole storage cascade. A suitably designed test rig where similar experiments in the form of cascades of coated honeycombs and foams can be performed has been built and further such tests are under way.Copyright © 2015 by ASME
06/28/2015 00:00:00
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7.4.3 Pure metal oxides (MO)
Investigation on Long Term Operation of Thermochemical Heat Storage with MgO-Based Composite Honeycombs
The efficient storing and utilizing of industrial waste heat can contribute to the reduction of CO2 and primary energy. Thermochemical heat storage uses a chemical and/or an adsorption-desorption reaction to store heat without heat loss. This study aims to assess the long-term operational feasibility of thermochemical material based composite honeycombs, so that a new thermochemical heat storage and peripheral system were prepared. The evaluation was done by three aspects: The compressive strength of the honeycomb, heat charging, and the discharging capabilities of the thermochemical heat storage. The compressive strength exceeded 1 MPa and is sufficient for safe use. The thermal performance was also assessed in a variety of ways during 100 cycles, 550 h in total. By introducing a new process, the amount of thermochemical-only charging was successfully measured for the first time. Furthermore, the heat charging capabilities were measured at 55.8% after the end of the experiment. Finally, the heat discharging capability was decreased until 60 cycles and there was no further degradation thereafter. This degradation was caused by charging at a too high temperature (550 °C). In comparative tests using a low temperature (450 °C), the performance degradation became slow, which means that it is important to find the optimal charging temperature.
04/02/2019 00:00:00
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7.4.4 Pure metal oxides (MO)
Revisiting the BaO2/BaO redox cycle for solar thermochemical energy storage
The barium peroxide-based redox cycle was proposed in the late 1970s as a thermochemical energy storage system. Since then, very little attention has been paid to such redox couples. In this paper, we have revisited the use of reduction–oxidation reactions of the BaO2/BaO system for thermochemical heat storage at high temperatures. Using thermogravimetric analysis, reduction and oxidation reactions were studied in order to find the main limitations associated with each process. Furthermore, the system was evaluated through several charge–discharge stages in order to analyse its possible degradation after repeated cycling. Through differential scanning calorimetry the heat stored and released were also determined. Oxidation reaction, which was found to be slower than reduction, was studied in more detail using isothermal tests. It was observed that the rate-controlling step of BaO oxidation follows zero-order kinetics, although at high temperatures a deviation from Arrhenius behaviour was observed probably due to hindrances to anionic oxygen diffusion caused by the formation of an external layer of BaO2. This redox couple was able to withstand several redox cycles without deactivation, showing reaction conversions close to 100% provided that impurities are previously eliminated through thermal pre-treatment, demonstrating the feasibility of this system for solar thermochemical heat storage.
01/01/2016 00:00:00
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7.4.5 Pure metal oxides (MO)
Screening of thermochemical systems based on solid-gas reversible reactions for high temperature solar thermal energy storage
A viable way to manage the inherently intermittent availability of solar energy in concentrated solar power plants is to store solar energy during on-sun hours to be able to use it later during off-sun hours, enabling on-demand electricity delivery. Thermochemical heat storage systems present some noteworthy advantages when compared with latent and sensible heat storage, namely (i) high energy storage density because the storage capacity by unit of mass or volume corresponding to the reaction enthalpy is generally high, (ii) heat storage at room temperature and long term energy storage because the products can be cooled and stored at room temperature without energy losses as heat can be stored indefinitely in chemical bonds, (iii) facility of transport because solid materials can be transferred over long distances, (iv) constant restitution temperature providing constant heat source because exothermic reactions are carried out at sufficiently high temperatures to generate electricity in constant conditions and therefore to produce a constant power. This paper presents an overview of the different potential thermochemical systems based on reversible solid-gas reactions operating at high temperatures and a screening of suitable materials that are interesting candidates in the 400–1200°C range for thermochemical heat storage in concentrated solar power systems. The most promising materials belonging to the metal oxides, hydroxides, and carbonates solid-gas systems are selected for experimental validation and further investigations.
10/01/2016 00:00:00
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7.4.6 Pure metal oxides (MO)
Thermochemical Heat Storage at High Temperatures using Mn2O3/Mn3O4 System: Narrowing the Redox Hysteresis by Metal Co-doping☆
Abstract Thermal energy storage systems are a key component of concentrated solar power plants, since its implementation increases the energy generation dispatchability. In particular, thermochemical storage through redox cycles of metal oxides is going to play a major role in future plants working with volumetric air receivers, as they are able to store energy at high temperatures, using air as both heat transfer fluid and reactant. One of the most remarkable characteristics of redox cycles of some metal oxides (e.g. Mn 2 O 3 /Mn 3 O 4 and Co 3 O 4 /CoO) is that the forward and reverse reactions start at different temperatures, i.e., a thermal hysteresis exists. Namely, the metal oxide reduction takes place at higher temperatures than the re-oxidation of the reduced phase. In the case of Mn-based redox couple, the temperature difference between reduction and oxidation is of ca. 200 °C, whereas for Co 3 O 4 /CoO is around 50 °C. Narrowing the hysteresis loop for the manganese oxide system means that heat is stored and released in a closer range of temperatures, which will suppose an increase of the charge-discharge energy efficiency. In this work, the effect that co-doping the Mn oxides with Fe and Cu has on the redox temperatures of both reactions has been studied. Materials were prepared by a variation of Pechini method and characterized by XRD and SEM. The capacity to withstand several redox cycles was analyzed by thermogravimetric analyses. It was found that addition of certain amount of both dopants narrowed the thermal hysteresis of such redox couple, presenting stable reversibility.
06/01/2015 00:00:00
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7.5 Zeolite

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Zeolites are crystalline alumino-silicates, characterized by a high specific surface area (i.e., about 800 m2/g) and wide microporous volumes, which make these materials perfectly suitable for water vapor adsorption. Owing to their porous structure, zeolites are usually highly hydrophilic, which allows them to obtain high adsorption capacities even at low partial pressures. This high affinity with water, of course, is reflective of strong bonding that requires higher temperatures to be broken compared to silica gels (i.e., more than 150 °C). Zeolites type A, 13X and Y are the most common classical synthetic zeolites employed for adsorption heat storage. These materials are mostly used for open adsorption TES, since, in order to get enough energy storage density, they must be regenerated at high temperatures, making air the most effective heat transfer medium. ***Applications:*** * Employed for industrial waste heat recovery and storage * Domestic seasonal storage

7.5.1 Zeolite
Hot tap water production by a 4 kW sorption segmented reactor in household scale for seasonal heat storage
Abstract Replacing fossil fuel by solar energy as a promising sustainable energy source, is of high interest, for both electricity and heat generation. However, to reach high solar thermal fractions and to overcome the mismatch between supply and demand of solar heat, long term heat storage is necessary. A promising method for long term heat storage is to use thermochemical materials, TCMs. The reversible adsorption–desorption reactions, which are exothermic in the hydration direction and endothermic in the reverse dehydration direction, can be used to store heat. A 250 L setup based on a gas–solid reaction between water–zeolite 13X is designed and tested. Humid air is introduced into a packed bed reactor filled with dehydrated material, and due to the adsorption of water vapour on TCM, heat is released. The reactor consists of four segments of 62.5 L each, which can be operated in different modes. The temperature is measured at several locations to gain insight into the effect of segmentation. Experiments are performeignore.txtd for hydration–dehydration cycles in different modes. Using the temperatures measured at different locations in the system, a complete thermal picture of the system is calculated, including thermal powers of the segments. A maximum power of around 4 kW is obtained by running the segments in parallel mode. Compactness and robustness are two important factors for the successful introduction of heat storage systems in the built environment, and both can be met by reactor segmentation. With the segmented reactor concept, a high flexibility can be achieved in the performance of a heat storage system, while still being compact. The system is also able to produce domestic hot tap water with the required temperature of 60 °C. This can be done by implementing a recuperating unit to preheat the inflow by recovering the residual heat in the outflow. In this work, the recuperator is simulated by a heater, and applicability of the system for domestic purposes is assessed. An energy density of 198 kWh/m 3 is calculated on material level, and the energy density calculated on reactor level is around 108 kWh/m 3 and 61 kWh/m 3 for experiment without and with preheating, respectively.
06/01/2018 00:00:00
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7.6 Silica Gel

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Silica gels historically represent one of the most employed adsorbent materials for water vapor adsorption. In fact, they represent a less expensive option for adsorption TES applications and can be easily employed for heat sources at temperatures lower than 100 °C (e.g., flat-plate solar thermal collectors). It is important to highlight that the porous structure of silica gels for closed adsorption TES must be completely different from that which is employed for open adsorption TES. Indeed, as in a closed system the adsorption/desorption process usually occurs in a limited partial pressure range (e.g., between 0.1 and 0.3 p/p0), it is necessary to have silica gels with highly microporous structures, capable of exchanging high quantities of water vapor. On the contrary, in an open adsorption TES, since the working partial pressures are usually higher, a mesoporous silica gel can be also employed, due to the capillary condensation phenomena that occurs within this working range. ***Applications:*** * 40 m² high performance solar panel collectors, two water tanks with 2 and 10 m³ and 26 ton silicagel can match the annual demand of 10.3 MWh of a single-family house


7.7 Zeo-like Materials

0

their crystalline structure is somewhat similar to those of classical zeolites. The two classes that showed the most promising features are the aluminophosphates (AlPOs) and the silico-aluminophosphates (SAPOs). Indeed, in contrast to other classical adsorbents, these materials show a partially hydrophobic behavior, that is reflected in an S-shaped adsorption isotherm. This is an advantageous characteristic, that allows a high amount of water vapor exchange to be obtained in a narrow range of partial pressure. Accordingly, since the overall heat storage capacity is highly dependent on the water vapor exchange, these materials can guarantee very high heat storage capacities. Among these two classes, the most attractive materials are known as AlPO-18 and SAPO-34


7.8 Composite

0

Composite sorbents represent a hybrid method to enhance the sorption ability of materials under the typical working boundary conditions of adsorption TES. Indeed, they are based on the embedding of inorganic salt (e.g., CaCl2, LiCl, LiBr) inside a host porous structure (e.g., silica gel, vermiculite, zeolites). More information also available [here](https://www.sciencedirect.com/science/article/pii/S1876610212015585) ***Applications:*** * Solar storage: A new concept for longterm solar storage is based on the absorption properties of aqueous calcium chloride. Water, diluted and concentrated calcium chloride solutions are stored in a single tank. An immersed heat exchanger and stratification manifold are used to preserve longterm sorption storage, and to achieve thermal stratification. The feasibility of the concept is demonstrated via measurements of velocity, CaCl2 mass fraction, and temperature in a 1500 liter prototype tank during sensible charging.

7.8.1 Composite
Buoyancy Driven Mass Transfer in a Liquid Desiccant Storage Tank
A new concept for long-term solar storage is based on the absorption properties of aqueous calcium chloride. Water, diluted and concentrated calcium chloride solutions are stored in a single tank. An immersed heat exchanger and stratification manifold are used to preserve long-term sorption storage, and to achieve thermal stratification. The feasibility of the concept is demonstrated via measurements of velocity, CaCl2 mass fraction, and temperature in a 1500 liter prototype tank during sensible charging. Experiments are conducted over a practical range of the relevant dimensionless parameters. For Rayleigh numbers from 3.4 × 108 to 5.6 × 1010 and buoyancy ratios from 0.8 to 46.2, measured Sherwood numbers are 11±2 to 62±9 and the tank is thermally stratified. Convective mixing is inhibited by the presence of a steep density gradient at the interface between regions of differing mass fraction. The predicted storage time scales for the reported Sherwood numbers are 160 to 902 days.Copyright © 2012 by ASME
07/23/2012 00:00:00
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7.9 Metal Hydrides

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A metal hydride energy store for CSP operates through the highly endothermic and exothermic processes of hydrogen desorption and absorption, respectively. The metal hydride in question (designated as the HT (high temperature) hydride) will be heated during a day-cycle from solar energy and will release hydrogen. This hydrogen gas must then be stored. The hydrogen can either be stored in a volumetric gas tank or another metal hydride that operates at LT (low temperature). ***Applications:*** * Concentrated solar power plants

7.9.1 Metal Hydrides
Complex metal hydrides for hydrogen, thermal and electrochemical energy storage
Hydrogen has a very diverse chemistry and reacts with most other elements to form compounds, which have fascinating structures, compositions and properties. Complex metal hydrides are a rapidly expanding class of materials, approaching multi-functionality, in particular within the energy storage field. This review illustrates that complex metal hydrides may store hydrogen in the solid state, act as novel battery materials, both as electrolytes and electrode materials, or store solar heat in a more efficient manner as compared to traditional heat storage materials. Furthermore, it is highlighted how complex metal hydrides may act in an integrated setup with a fuel cell. This review focuses on the unique properties of light element complex metal hydrides mainly based on boron, nitrogen and aluminum, e.g., metal borohydrides and metal alanates. Our hope is that this review can provide new inspiration to solve the great challenge of our time: efficient conversion and large-scale storage of renewable energy.
10/18/2017 00:00:00
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7.9.2 Metal Hydrides
Hydrogen storage systems based on magnesium hydride: from laboratory tests to fuel cell integration
The paper reviews the state of the art of hydrogen storage systems based on magnesium hydride, emphasizing the role of thermal management, whose effectiveness depends on the effective thermal conductivity of the hydride, but also depends of other limiting factors such as wall contact resistance and convective exchanges with the heat transfer fluid. For daily cycles, the use of phase change material to store the heat of reaction appears to be the most effective solution. The integration with fuel cells (1 kWe proton exchange membrane fuel cell and solid oxide fuel cell) highlights the dynamic behaviour of these systems, which is related to the thermodynamic properties of MgH2. This allows for “self-adaptive” systems that do not require control of the hydrogen flow rate at the inlet of the fuel cell.
02/01/2016 00:00:00
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7.10 Ammonia storage tanks

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The electricity is first transformed into the chemical potential of the working fluid by means of varying the refrigerant or absorbent mass fraction in the working fluid storage tank. When cooling, heating or dehumidifying is needed, the potential stored in the tank can then be transformed into cold/heat energy by means of absorption refrigeration/heat pump or into dehumidification/desiccation energy by means of absorption dehumidification. Liquid ammonia is stored either at ambient temperature under high pressure or at -33°C under atmospheric pressure. (The description liquefied is also sometimes used for liquid, see Glossary for explanation). In some cases, it is also stored at intermediate temperatures and pressures (semi-refrigerated). For pressure vessels, the inspection requirements in most countries are governed by the respective pressure vessel codes and regulations. The recommendations provided in this Guidance are, therefore, limited to atmospheric pressure storage tanks, which operate at -33°C. Amonia can also be used as In the ammonia-based thermal energy storage system, liquid ammonia (NH3) is dissociated in an energy storing (endothermic) chemical reactor as it absorbs solar thermal energy. At a later time, the gaseous products hydrogen (H2) and nitrogen (N2) are reacted on demand in an energy releasing (exothermic) reactor to resynthesise ammonia and recover the stored solar energy. Because the solar energy is stored in a chemical form at ambient temperature, there are no energy losses in the store regardless of the length of time that the reactants remain in storage. The reactors are packed with standard commercial catalyst materials to promote both reactions. Counter-flow heat exchangers transfer heat between in-going and out-going reactants at each reactor to use the energy most effectively. Apart from the ability of the ammonia system to allow for solar energy storage, other advantages, that are not necessarily shared by other solar thermochemical or photochemical systems, make this process unique. ***Applications:*** * Large scale energy storage

7.10.1 Ammonia storage tanks
Variable mass energy transformation and storage (VMETS) system using NH3-H2O as working fluid. Part 2: Modeling and simulation under partial storage strategy
This paper presents a new variable mass energy transformation and storage (VMETS) system using ammonia–water solution (NH3–H2O) as working fluid. The system has a wide range of working temperature. It can be used to shift load with a diurnal energy storage system for cooling in summer, heating in winter, or hot water supplying all year long. It can also be used to store refrigerating energy for various industrial and commercial applications. The key to the system is to regulate the chemical potential by controlling the refrigerant mass fraction in the working fluid with respect to time. As a result, by using a solution storage tank and an ammonia storage tank, the energy transformation and storage can be performed at the desirable time to provide low cost cooling and heating efficiently. As the first part of our study, this paper presents the principle and dynamic models of the VMETS system and performs the numerical simulation when the system works in the cooling and heating modes, respectively, under the full storage strategy. The simulation predicts the dynamic behavior of the VMETS system under various operation conditions and shows that the VMETS system for cooling in summer is also suitable for heating in winter or for hot water supplying all year long by adjusting the initial solution concentration. The energy conversion efficiency of the system is larger than that of conventional thermal energy storage (TES) systems, especially under the condition of system operation for heating or hot water supplying in the heating mode. These simulation results are very helpful for detailed design and control of the system. To investigate the system performance under the partial storage strategy, modeling and numerical simulation will be performed in a subsequent paper.
01/01/2007 00:00:00
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