Heat exchangers
Scout intake sheet
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 exchangers. These technologies can be used for liquid-liquid, gas-gas or gas-liquid heat exchanges. Of interest are the material (ex: corrosion resistance), the efficiency, the capacity, the temperature and the size. The search should focus on integrated and applied systems (i.e. no lab searches on materials).
Scope
Current known technique(s)
- Flat plate
- shell and tube
- Heat pipe
- 3d printing
Ideal outcome
- Flat plate
- shell and tube
- Heat pipe
- 3d printing
An overview of all the existing heat exchangers with their specification and suppliers
Minimum viable outcome
A list of all the existing heat exchangers
Objective(s)
- Max (working) Pressure
- Material
- Effectiveness
- Max. design temperature (°C)
- Sizing of the equipment
Constraint(s)
- Capacity
Functions
Action = [exchange] OR [is] OR [design] OR [obtain] OR [review] OR [review] OR [know] OR [use]
Object = [heat] OR [heat exchanger] OR [heat exchanger] OR [heat transfer] OR [heat exchanger] OR [heat] OR [boiling heat transfer mechanism] OR [nanofluid]
Environment =
[gas gas] OR [heat exchange] OR [tube] OR [shell] OR [flow] OR [process] OR [design] OR [fluid flow] OR [heat transfer] OR [pressure drop] OR [heat exchanger type] OR [heat transfer mechanism] OR [new concept] OR [shell] OR [algorithm] OR [industrial] OR [compact] OR [nanofluid] OR [review]
Terminology
- HX / HEX
Preliminary Results
Concept | Technology | Selection | |
---|---|---|---|
1 Plate
Plate heat exchangers use the surface of plates (usually stacked) to exchange heat. They are commonly used because of their compactness, ease of production, sensitivity, easy care after set-up and efficiency. Plate type heat exchangers are widely used in process industries for gas/gas applications. Typically, these exchangers prove to be very efficient, especially as air preheaters in process furnaces or in equipment used in environmental protection.
|
1.1 Brazed plate heat exchanger (BPHE) |
|
0 of 0 |
1.2 Gasketed plate heat exchanger (GPHE) |
|
0 of 0 | |
1.3 Welded plate heat exchanger (WPHE) |
|
0 of 0 | |
1.4 Spiral plate heat exchangers (SPHE) |
|
0 of 0 | |
1.5 Printed circuit heat exchanger (PCHE) |
|
0 of 0 | |
1.6 Pillow-plate heat exchangers (PPHE) |
|
0 of 0 | |
1.7 Plate and Shell heat exchanger |
|
0 of 0 | |
1.8 Scraped-surface heat exchangers (SSHE) |
|
0 of 0 | |
1.9 Wide-gap plate heat exchanger |
|
0 of 0 | |
1.10 Capsule-type plate heat exchanger |
|
0 of 0 | |
2 Shell and Tube
A shell and tube heat exchanger is a class of heat exchanger designs. It is the most common type of heat exchanger in oil refineries and other large chemical processes, and is suited for higher-pressure applications. As its name implies, this type of heat exchanger consists of a shell (a large pressure vessel) with a bundle of tubes inside it. One fluid runs through the tubes, and another fluid flows over the tubes (through the shell) to transfer heat between the two fluids. The set of tubes is called a tube bundle. [Wiki](https://en.wikipedia.org/wiki/Shell_and_tube_heat_exchanger)
There are different design elements that can be used in a shell and tube:
- Baffles: Baffles can be used in the shell to break up or split the flow to increase transfer; some specific types are described in the technologies.
- Floating headers: floating headers can be used when thermal expansion is an issue.
- Tube design: specific tube design is described in the technologies.
|
2.1 Shell and Tube Designs (TEMA) |
|
0 of 0 |
2.2 Flat tubes heat exchanger |
|
0 of 0 | |
2.3 Twisted tube heat exchanger |
|
0 of 0 | |
2.4 Multipass-type heat exchanger |
|
0 of 0 | |
2.5 Falling-film heat exchanger |
|
0 of 0 | |
2.6 Helical baffled heat exchanger |
|
0 of 0 | |
2.7 ROD baffled heat exchanger |
|
0 of 0 | |
3 Other tubular
Next to shell and tube heat exchangers, other tubular heat exchangers are presented.
|
3.1 Double pipe heat exchanger (DPHE) |
|
0 of 0 |
3.2 Triple concentric tube heat exchanger (TCTHE) |
|
0 of 0 | |
3.3 Helical coil heat exchanger |
|
0 of 0 | |
3.4 Spiral wound heat exchanger (SWHE) |
|
0 of 0 | |
4 Extended or Enhanced
Extended or enhanced heat exchangers make use of design elements that enhance heat transfer, usually by etending the surface area.
|
4.1 Plate-fin heat exchanger |
|
0 of 0 |
4.2 Finned tube heat exchanger |
|
0 of 0 | |
4.3 Plate-fin-and-tube heat exchanger |
|
0 of 0 | |
4.4 Corrugated plate heat exchanger |
|
0 of 0 | |
4.5 Coil wired tube heat exchanger |
|
0 of 0 | |
4.6 Twisted-tape tube heat exchanger |
|
0 of 0 | |
4.7 Rotor enhanced shell and tube |
|
0 of 0 | |
4.8 Metal foam heat exchangers |
|
0 of 0 | |
5 Regenerative
A regenerative heat exchanger, or more commonly a regenerator, is a type of heat exchanger where heat from the hot fluid is intermittently stored in a thermal storage medium before it is transferred to the cold fluid. To accomplish this the hot fluid is brought into contact with the heat storage medium, then the fluid is displaced with the cold fluid, which absorbs the heat.
|
5.1 Fixed matrix heat exchanger |
|
0 of 0 |
5.2 Rotary heat exchanger |
|
0 of 0 | |
5.3 Rotating hood regenerator |
|
0 of 0 | |
5.4 Microscale regenerative heat exchanger |
|
0 of 0 | |
6 Direct contact
Direct contact heat exchangers involve heat transfer between hot and cold streams of two phases in the absence of a separating wall. Thus such heat exchangers can be classified as:
- Gas – liquid
- Immiscible liquid – liquid
- Solid-liquid or solid – gas
Most direct contact heat exchangers fall under the Gas – Liquid category, where heat is transferred between a gas and liquid in the form of drops, films or sprays.
|
6.1 Gas-solid heat exchangers |
|
0 of 0 |
6.2 Spray column |
|
0 of 0 | |
6.3 Tray column |
|
0 of 0 | |
6.4 Bubble column |
|
0 of 0 | |
7 Compact
Compact heat exchangers are becoming increasingly important elements in many industrial processes, both in their original role as contributors to increased energy efficiency, and more recently as the basis for novel ‘intensified' unit operations.
|
7.1 Microchannel heat exchanger |
|
0 of 0 |
7.2 Hollow fiber heat exchanger |
|
0 of 0 | |
7.3 Meso heat exchanger |
|
0 of 0 | |
7.4 Microjet heat exchanger |
|
0 of 0 | |
7.5 Marbond heat exchanger |
|
0 of 0 | |
8 Trends
There are some trends in heat exchangers that affect their design or material use.
|
8.1 3D printed heat exchangers |
|
0 of 0 |
8.2 Nano fluids-based |
|
0 of 0 | |
8.3 Polymer heat exchangers |
|
0 of 0 | |
8.4 Phase change material heat exchange |
|
0 of 0 |
Published 07/31/2019
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 exchange heat. Heat exchangers can be classified in a number of ways, inclucing transfer mechanisms, type of contact, direction of flow, phases and construction. To give the broadest overview of integrated system the heat exchangers are classified based on design. 8 concepts are distinguished based on the results: 1 Plate heat exchangers 2 Shell and Tube heat exchangers 3 Other tubular heat exchangers 4 Extended or Enhanced heat exchangers 5 Regenerative heat exchangers 6 Direct contact heat exchangers 7 Compact heat exchangers 8 Trends in heat exchangers Every concept comprises multiple design types (46 in total). Within these type there are even more design possibilities for some of the heat exchangers. 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.
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 Plate
Plate heat exchangers use the surface of plates (usually stacked) to exchange heat. They are commonly used because of their compactness, ease of production, sensitivity, easy care after set-up and efficiency. Plate type heat exchangers are widely used in process industries for gas/gas applications. Typically, these exchangers prove to be very efficient, especially as air preheaters in process furnaces or in equipment used in environmental protection.
|
1.1 Brazed plate heat exchanger (BPHE) |
|
0 of 0 |
1.2 Gasketed plate heat exchanger (GPHE) |
|
0 of 0 | |
1.3 Welded plate heat exchanger (WPHE) |
|
0 of 0 | |
1.4 Spiral plate heat exchangers (SPHE) |
|
0 of 0 | |
1.5 Printed circuit heat exchanger (PCHE) |
|
0 of 0 | |
1.6 Pillow-plate heat exchangers (PPHE) |
|
0 of 0 | |
1.7 Plate and Shell heat exchanger |
|
0 of 0 | |
1.8 Scraped-surface heat exchangers (SSHE) |
|
0 of 0 | |
1.9 Wide-gap plate heat exchanger |
|
0 of 0 | |
1.10 Capsule-type plate heat exchanger |
|
0 of 0 | |
2 Shell and Tube
A shell and tube heat exchanger is a class of heat exchanger designs. It is the most common type of heat exchanger in oil refineries and other large chemical processes, and is suited for higher-pressure applications. As its name implies, this type of heat exchanger consists of a shell (a large pressure vessel) with a bundle of tubes inside it. One fluid runs through the tubes, and another fluid flows over the tubes (through the shell) to transfer heat between the two fluids. The set of tubes is called a tube bundle. [Wiki](https://en.wikipedia.org/wiki/Shell_and_tube_heat_exchanger)
There are different design elements that can be used in a shell and tube:
- Baffles: Baffles can be used in the shell to break up or split the flow to increase transfer; some specific types are described in the technologies.
- Floating headers: floating headers can be used when thermal expansion is an issue.
- Tube design: specific tube design is described in the technologies.
|
2.1 Shell and Tube Designs (TEMA) |
|
0 of 0 |
2.2 Flat tubes heat exchanger |
|
0 of 0 | |
2.3 Twisted tube heat exchanger |
|
0 of 0 | |
2.4 Multipass-type heat exchanger |
|
0 of 0 | |
2.5 Falling-film heat exchanger |
|
0 of 0 | |
2.6 Helical baffled heat exchanger |
|
0 of 0 | |
2.7 ROD baffled heat exchanger |
|
0 of 0 | |
3 Other tubular
Next to shell and tube heat exchangers, other tubular heat exchangers are presented.
|
3.1 Double pipe heat exchanger (DPHE) |
|
0 of 0 |
3.2 Triple concentric tube heat exchanger (TCTHE) |
|
0 of 0 | |
3.3 Helical coil heat exchanger |
|
0 of 0 | |
3.4 Spiral wound heat exchanger (SWHE) |
|
0 of 0 | |
4 Extended or Enhanced
Extended or enhanced heat exchangers make use of design elements that enhance heat transfer, usually by etending the surface area.
|
4.1 Plate-fin heat exchanger |
|
0 of 0 |
4.2 Finned tube heat exchanger |
|
0 of 0 | |
4.3 Plate-fin-and-tube heat exchanger |
|
0 of 0 | |
4.4 Corrugated plate heat exchanger |
|
0 of 0 | |
4.5 Coil wired tube heat exchanger |
|
0 of 0 | |
4.6 Twisted-tape tube heat exchanger |
|
0 of 0 | |
4.7 Rotor enhanced shell and tube |
|
0 of 0 | |
4.8 Metal foam heat exchangers |
|
0 of 0 | |
5 Regenerative
A regenerative heat exchanger, or more commonly a regenerator, is a type of heat exchanger where heat from the hot fluid is intermittently stored in a thermal storage medium before it is transferred to the cold fluid. To accomplish this the hot fluid is brought into contact with the heat storage medium, then the fluid is displaced with the cold fluid, which absorbs the heat.
|
5.1 Fixed matrix heat exchanger |
|
0 of 0 |
5.2 Rotary heat exchanger |
|
0 of 0 | |
5.3 Rotating hood regenerator |
|
0 of 0 | |
5.4 Microscale regenerative heat exchanger |
|
0 of 0 | |
6 Direct contact
Direct contact heat exchangers involve heat transfer between hot and cold streams of two phases in the absence of a separating wall. Thus such heat exchangers can be classified as:
- Gas – liquid
- Immiscible liquid – liquid
- Solid-liquid or solid – gas
Most direct contact heat exchangers fall under the Gas – Liquid category, where heat is transferred between a gas and liquid in the form of drops, films or sprays.
|
6.1 Gas-solid heat exchangers |
|
0 of 0 |
6.2 Spray column |
|
0 of 0 | |
6.3 Tray column |
|
0 of 0 | |
6.4 Bubble column |
|
0 of 0 | |
7 Compact
Compact heat exchangers are becoming increasingly important elements in many industrial processes, both in their original role as contributors to increased energy efficiency, and more recently as the basis for novel ‘intensified' unit operations.
|
7.1 Microchannel heat exchanger |
|
0 of 0 |
7.2 Hollow fiber heat exchanger |
|
0 of 0 | |
7.3 Meso heat exchanger |
|
0 of 0 | |
7.4 Microjet heat exchanger |
|
0 of 0 | |
7.5 Marbond heat exchanger |
|
0 of 0 | |
8 Trends
There are some trends in heat exchangers that affect their design or material use.
|
8.1 3D printed heat exchangers |
|
0 of 0 |
8.2 Nano fluids-based |
|
0 of 0 | |
8.3 Polymer heat exchangers |
|
0 of 0 | |
8.4 Phase change material heat exchange |
|
0 of 0 |
1 Plate
BackPlate heat exchangers use the surface of plates (usually stacked) to exchange heat. They are commonly used because of their compactness, ease of production, sensitivity, easy care after set-up and efficiency. Plate type heat exchangers are widely used in process industries for gas/gas applications. Typically, these exchangers prove to be very efficient, especially as air preheaters in process furnaces or in equipment used in environmental protection.
1.1 Brazed plate heat exchanger (BPHE)
A brazed plate heat exchanger (BPHE) is built up from a package of corrugated stainless steel plates which are brazed together using materials such as copper and nickel. The plate package is generally sealed by front and rear plate packages to form a self contained unit. Each plate has a characteristic corrugation pattern that governs the degree of thermal efficiency and hydraulic behavior of the BPHE unit. Further, four to six apertures are placed in the corners/edges of these plates. Alternate plates are arranged at 180° to each other resulting in formation of the inlet and outlet port manifolds for the various process fluid circuits. [#ARTNUM](#article-26232-1752739663).
Compactness, low volume, scalability, possibility to achieve close temperature approaches,
relatively high values of the heat transfer coefficients make brazed plate heat exchangers
suitable for a very wide range of applications. Plate heat exchangers are widely used for phase-change heat transfer in refrigeration, residential heating and air-conditioning applications. [#ARTNUM](#article-26232-1752739663). They are also employed in natural gas liquefaction (LNG) plants. [#ARTNUM](#article-26232-2792430176) They are used especially when corrosion can be an issue. In Brazed Plate Heat Exchangers, the brazing process eliminates gasketed joints which allows for higher design pressure and temperatures. [Source](http://www.graham-mfg.com/gasketed-and-brazed-plate-heat-exchanger-advantages)
1.2 Gasketed plate heat exchanger (GPHE)
In Gasketed Plate Heat Exchangers, each heat transfer plate is fitted with an elastomeric gasket, which seals and distributes the process fluids. The heads, normally referred to as channel covers, include connections to permit the entry of the process fluid into the plate pack. [Source](http://www.graham-mfg.com/gasketed-and-brazed-plate-heat-exchanger-advantages) The plates can easily be removed for cleaning, expansion, or replacing purposes, drastically reducing maintenance costs. Gasketed Plate Heat Exchangers are limited in high fluid temperatures, by the temperature limitations of the gasket. [Source](https://www.thermaxxjackets.com/plate-and-frame-heat-exchangers-explained/)
GPHE are employed in direct heating and HVAC applications.
Suppliers
1.3 Welded plate heat exchanger (WPHE)
Welded plate heat exchangers are similar to Gasketed plate heat exchangers, but instead the plates are welded together. They are extremely durable, and are ideal for transferring fluids with high temperatures or corrosive materials. The plates are all welded together in one block, they therefore can’t be fully dismantled and the heating/cooling capacity is fixed. However, they do allow higher pressure and temperature fluids to be used so you’ll find these mostly in heavy industrial, power plants and oil refinery applications. [Source](https://theengineeringmindset.com/plate-heat-exchanger-applications/)
Typical applications of module welded plate heat exchangers in the chemical industry are acid coolers, thermal oil coolers, or condensers for hydrocarbon mixtures.[#ARTNUM](#article-26241-2062888851)
1.4 Spiral plate heat exchangers (SPHE)
The main advantage of the SHE is its highly efficient use of space. This attribute is often leveraged and partially reallocated to gain other improvements in performance, according to well known tradeoffs in heat exchanger design. (A notable tradeoff is capital cost vs operating cost.) A compact SHE may be used to have a smaller footprint and thus lower all-around capital costs, or an oversized SHE may be used to have less pressure drop, less pumping energy, higher thermal efficiency, and lower energy costs. The Spiral heat exchanger is good for applications such as pasteurization, digester heating, heat recovery, pre-heating (see: recuperator), and effluent cooling. For sludge treatment, SHEs are generally smaller than other types of heat exchangers. [Wiki](https://en.wikipedia.org/wiki/Heat_exchanger#Helical-coil_heat_exchangers)
A SPHE consists of two sheets that are rolled around a central rod and therefore two separated concentric channels are made. The ends of the channels are sealed through welding. There are two possibilities to seal the sides of the heat exchanger: using bolts and gaskets to fasten the covering sheets to the heat exchanger or welding the covering sheets to the heat exchanger. [#ARTNUM](#article-26228-2342724403)
**Research findings:**
- Spiral heat exchanger is a self cleaning equipment with low fouling tendencies, easily accessible for inspection or mechanical cleaning and with minimum space requirements. [#ARTNUM](#article-26228-2065526122)
1.5 Printed circuit heat exchanger (PCHE)
PCHE is a plate-type compact heat exchanger and its core is composed of thin plates (of thickness1.5–3 mm) made of alloys like stainless steel or inconel alloys [3], with flow channels etched on them by chemical etching process. The etched plates are stacked one over the other and are bonded together using diffusion bonding. These blocks are welded together to construct the core of the PCHE and the headers are connected to the core for external connections. Printed Circuit Heat Exchanger (PCHE) is a widely chosen plate type compact heat exchanger for high pressure applications.[#ARTNUM](#article-26243-2767695692)
The complete microchannel heat exchangers are highly compact, typically comprising about onefifth the size and weight of conventional heat exchangers for the same thermal duty and pressure drops. PCHEs can be constructed out of a range of materials, including austenitic stainless steels suitable for design temperatures up to 800°C, and nickel alloys such as Incoloy 800HT suitable for design temperatures more than 900°C. Single units ranging from a few grams up to 100 tonnes have been manufactured. [#ARTNUM](#article-26243-1980144440)
The field of applications is very varied, including specialised chemicals processing, and PCHEs are even to be found orbiting the Earth in the International Space Station! Due to the inherent flexibility of the etching process, the basic construction may readily be applied to both a wider range, and more complex integration of process unit operations. Chemical reaction, rectification, stripping, mixing, and absorption, as well as boiling and condensation, can be incorporated into compact integrated process modules.[#ARTNUM](#article-26243-1980144440)
1.6 Pillow-plate heat exchangers (PPHE)
The pillow plate is constructed using a thin sheet of metal spot-welded to the surface of another thicker sheet of metal. The thin plate is welded in a regular pattern of dots or with a serpentine pattern of weld lines. After welding the enclosed space is pressurised with sufficient force to cause the thin metal to bulge out around the welds, providing a space for heat exchanger liquids to flow, and creating a characteristic appearance of a swelled pillow formed out of metal. A pillow plate exchanger is commonly used in the dairy industry for cooling milk in large direct-expansion stainless steel bulk tanks. The pillow plate allows for cooling across nearly the entire surface area of the tank, without gaps that would occur between pipes welded to the exterior of the tank. [Wiki](https://en.wikipedia.org/wiki/Heat_exchanger#Helical-coil_heat_exchangers)
Pillowplate heat exchangers (PPHE) are a novel heat exchanger type based on wavy pillowlike plate geometry. Typically, they are composed of parallel plates arranged as a stack. In this way, inner channels within the pillowplates alternate with outer channels between the adjacent plates, and thus, a structure with alternating inner and outer channels is arranged for the heat transfer media. In heat exchanger applications, several pillow-plates are arranged vertically as a stack, parallel to each other, with alternating channels within and between the pillow-plates. The medium inside the pillow-plates is being continuously redirected by the welding point pattern. This leads to thin boundary layers and good heat transfer performance, and hence, to lower required heat transfer area and lower investment. On the other hand, internal pressure loss also increases, leading to high operating costs for pumps and compressors. [#ARTNUM](#article-26310-2779667980)
Suppliers
1.7 Plate and Shell heat exchanger
The plate and shell heat exchanger combines the plate heat exchanger with shell and tube heat exchanger technologies. The heart of the heat exchanger contains a fully welded circular plate pack made by pressing and cutting round plates and welding them together. Nozzles carry flow in and out of the platepack (the 'Plate side' flowpath). The fully welded platepack is assembled into an outer shell that creates a second flowpath ( the 'Shell side'). Plate and shell technology offers high heat transfer, high pressure, high operating temperature, uling and close approach temperature. In particular, it does completely without gaskets, which provides security against leakage at high pressures and temperatures. [Wiki](https://en.wikipedia.org/wiki/Heat_exchanger#Plate_and_shell_heat_exchanger)
Plate-and-shell exchangers combine the pressure and temperature capabilities of a cylindrical shell with the excellent heat transfer performance of a plate heat exchanger. The round plates ensure an even distribution of mechanical loads, without the stress concentrations that occur in the corners of rectangular plates.
Suppliers
1.8 Scraped-surface heat exchangers (SSHE)
An SSHE basically consists of a cylindrical rotating shaft (the “rotor”) within a concentric hollow stationary cylinder (the “stator”) so as to form an annular region along which the process fluid is pumped. The stator acts as the heat-transfer surface, and it is normally enclosed within another cylindrical tube which provides a gap through which a heating or cooling service fluid (for example, steam or ammonia) passes. Attached to the rotor are a number of pivoted blades, each of which scrapes the heat-transfer surface, removing processed fluid and hence allowing unprocessed fluid to come closer to the stator. A cut-away schematic of a typical SSHE is shown in the figure.
Scraped-surface heat exchangers (SSHEs) are extensively used in a wide variety of industrial settings where the continuous processing of fluids and fluid-like materials is involved. They are often used in the pharmaceutical and chemical industries (for example, in dewaxing oils and producing paints); however, they are most commonly found within the food-manufacturing sector, where they are used for mixing and heating or cooling foodstuffs during processes such as sterilisation, crystallisation and gelatinisation. Unlike the simpler plate heat exchangers which are commonly used for low-viscosity process fluids, SSHEs are designed to deal with the problems that arise when processing very viscous products.[#ARTNUM](#article-26537-2014080855)
Suppliers
1.9 Wide-gap plate heat exchanger
The wide gap heat exchanger is similar to a gasketed heat exchangers, accept that one or more of the channels are wider. It has excellent heat transfer and a compact structure with deeper corrugation, therefore,it is especially suitable for heat exchanging between fibrous and viscous materials/fluids and solid particle containing fluids.[#ARTNUM](#article-26309-2377641195).
Supplier
1.10 Capsule-type plate heat exchanger
The capsule-type plate heat exchanger is proposed to address high viscosity fluid which has concave and convex ellipsoidal embossing similar to half capsules[#ARTNUM](#article-26138-2503965242) and has the advantages of low pressure drop and less deposition due to the straight passages in the channels. [#ARTNUM](#article-26138-2914453957)
2 Shell and Tube
BackA shell and tube heat exchanger is a class of heat exchanger designs. It is the most common type of heat exchanger in oil refineries and other large chemical processes, and is suited for higher-pressure applications. As its name implies, this type of heat exchanger consists of a shell (a large pressure vessel) with a bundle of tubes inside it. One fluid runs through the tubes, and another fluid flows over the tubes (through the shell) to transfer heat between the two fluids. The set of tubes is called a tube bundle. [Wiki](https://en.wikipedia.org/wiki/Shell_and_tube_heat_exchanger)
There are different design elements that can be used in a shell and tube:
- Baffles: Baffles can be used in the shell to break up or split the flow to increase transfer; some specific types are described in the technologies.
- Floating headers: floating headers can be used when thermal expansion is an issue.
- Tube design: specific tube design is described in the technologies.
2.1 Shell and Tube Designs (TEMA)
A shell and tube heat exchanger is a class of heat exchanger designs. It is the most common type of heat exchanger in oil refineries and other large chemical processes, and is suited for higher-pressure applications. [Wiki](https://en.wikipedia.org/wiki/Shell_and_tube_heat_exchanger)
There are different design elements that can be used in a shell and tube, the Tubular Exchanger Manufacturer’s Association (TEMA) has provided standard nomenclature for describing different configurations of common shell & tube heat exchangers, as can be seen in the figure. [Source](https://www.engineeringpage.com/heat_exchangers/tema.html)
Links
2.2 Flat tubes heat exchanger
Flat tube heat exchangers use flat tubes. This can result in better heat transfer, especially when other design elements, like fins or vortex generators are used. Flat tubes are often used in cooling applications.
**Research findings:**
The heat exchanger element with flat tubes and vortex generators gives nearly twice as much heat transfer and only half as much pressure loss as the corresponding heat exchanger element with round tubes.
2.3 Twisted tube heat exchanger
A twisted (oval) tube heat exchanger is a type of heat exchanger that aims at improving the heat transfer coefficient of the tube side and also decreasing the pressure drop of the shell side. Tubes that play an important role in this heat transfer enhancement technique are made from normal round tubes. They are formed into an oval section with a superimposed twist by some special techniques. Two ends of the tubes remain round on the consideration of assembling them with the tube sheet. [#ARTNUM](#article-26126-2049240625)
**Research findings:**
The analyzing result shows that the twisted oval tube heat exchangers is preferred to work at low tube side flow rate and high shell side flow rate.
2.4 Multipass-type heat exchanger
In a multipass type heat exchanger one fluid moves through the shell multiple times, usually through the use of U-tubes. Multiple-pass shell-and-tube heat exchangers allow thermal expansion and easy mechanical cleaning, as well as longer flowpaths for a given exchanger length. In addition, the high velocities achieved for the tube fluid help increase heat transfer coefficients and reduce surface fouling. [#ARTNUM](#article-26148-1985475579)
Using multipass systems, gives more flexibilty in optimising fluid velocity, pressure drop and heat transfer.
Industries:
- Industrial waste heat recovery solutions
- Energy
- Oil and gas industry
- Chemical industry
2.5 Falling-film heat exchanger
A falling-film heat exchanger is characterized by one fluid forming a film on the inside of a tube, while being cooled or heated from the shell side. Usually the film is facilitated by gravity (vertically), although other types do exist.
It is often used as an evaporator in industry, to concentrate solutions. [Wiki](https://en.wikipedia.org/wiki/Falling_film_evaporator)
Suppliers
2.6 Helical baffled heat exchanger
The efforts to improve the shell side flow characteristics are made using the spiral baffle plates instead of vertical baffle plates. In this type of heat exchanger, fluid contacts with tubes flowing rotationally in the shell. It could improve heat exchanger performance considerably because stagnation portions in the shell could be removed. It is proved that the shell-and-tube heat exchanger with spiral baffle plates is superior to the conventional heat exchanger in terms of heat transfer.[#ARTNUM](#article-26213-1536994987)
2.7 ROD baffled heat exchanger
The ROD baffle heat exchanger can slightly enhance the shell side heat transfer coefficient with the significant reduction of pressure loss due to the shell side fluid flowing longitudinally through tube bundle, which leads to the reduction of the manufacture and running cost and in some cases to the dimensions reduction of the heat exchangers. [#ARTNUM](#article-26129-2047878495)
The RODbaffle exchanger offers a solution to the vexing problem of tube failures in shell-and-tube exchangers resulting from tube vibration.
Supplier
3 Other tubular
BackNext to shell and tube heat exchangers, other tubular heat exchangers are presented.
3.1 Double pipe heat exchanger (DPHE)
One of the most simple and applicable heat exchangers is double pipe heat exchanger (DPHE), also called the concentric tube heat exchanger. This kind of heat exchanger is widely used in chemical, food, oil and gas industries. Upon having a relatively small diameter, many precise researches have also hold firmly the belief that this type of heat exchanger is used in high-pressure applications. They are also of great importance where a wide range of temperature is needed. [#ARTNUM](#article-26215-2519485646)
- The performance of the heat exchanger and the pressure drop are in a close interaction with the geometry. [#ARTNUM](#article-26215-2771080156)
3.2 Triple concentric tube heat exchanger (TCTHE)
In the TCTHE, there are three sections: central tube, inner annular space and
outer annular space. Heat transfer mediums are passed through the central tube and outer annularspace and a thermal fluid is passed through an inner annular space.
The triple tube heat exchanger contributes higher heat exchanger effectiveness and more energy saving compared with double tube heat exchanger per unit length.[#ARTNUM](#article-26134-2245358019)
3.3 Helical coil heat exchanger
Helical coil heat exchangers contain a helical tube. They are a simpler version of a spiral wound heat exchanger.
Helical coils are very alluring for various processes such as heat exchangers and reactors because they can accommodate a large heat transfer area in a small space, with high heat transfer coefficients and narrow residence time distributions.
The modification of the flow in the helically coiled tubes is due to the centrifugal forces. The curvature of the tube produces a secondary flow field with a circulatory motion, which pushing the fluid particles toward the core region of the tube. Thus the application of curved tubes in heat exchange process can be highly beneficial in comparison with the straight tube. These applications can arise in the food processing industry for heating and cooling of highly viscous liquid food, such as pastes, or for products that are sensitive to high shear stresses.
**Advantages:**
- Heat transfer rate in helical coil are higher as compared to a straight tube heat exchanger. Compact
structure.
- It requires small amount of floor area compared to other heat exchangers.
- Larger heat transfer surface area.
**Applications:**
- Heat exchangers with helical coils are widely used in industries. The most common industries where heat
exchangers are used a lot are power generation plants, nuclear plants, process plants, refrigeration, heat
recovery systems, food processing industries, etc.
- Helical coil heat exchanger is used for residual heat removal system in islanded or barge mounted nuclear
reactor system, where nuclear energy is used for desalination of sea water.
- In cryogenic applications including LNG plant. [#ARTNUM](#article-26208-2593188271)
3.4 Spiral wound heat exchanger (SWHE)
A spiral wound heat exchanger is very compact heat exchanger composed of spiralled coils. It can be used in a shell and tube type of exchanger. They can also be used for multi-phase and multi stream applications.
**Research findings:**
- Spiral wound heat exchanger (SWHE) has been used as the main cryogenic heat exchanger in 90% of land-based liquefied natural gas (LNG) plants, due to the advantages of compact structure, high pressure resistance, large scaleunit, good thermal compensation performance and multi-stream heat transfer capability. [#ARTNUM](#article-26124-2748655173)
- A spiral-wound heat exchanger (SWHE) has many significant advantages over other heat exchangers, such as high robustness, high effectiveness and large exchanger area per volume. As such, it has been widely used in liquefied natural gas (LNG) plants, air separation plants, petroleum plants and nuclear reactor plants. Especially in the large-scale land-based LNG plants and offshore floating LNG plants, the SWHE is the preferred choice of the main cryogenic heat exchanger. [#ARTNUM](#article-26124-2774313722)
Suppliers
4 Extended or Enhanced
BackExtended or enhanced heat exchangers make use of design elements that enhance heat transfer, usually by etending the surface area.
4.1 Plate-fin heat exchanger
A plate-fin heat exchanger is a form of compact heat exchanger consisting of a block of alternating layers of corrugated fins and flat separators known as parting sheets. These heat exchangers can be made in a variety of materials such as aluminium, stainless steels, nickel, copper, etc. depending upon the operating temperatures and pressures. They are widely used in aerospace, automobile and cryogenic industries due to its compactness (i.e., high heat transfer surface area-to-volume ratio) for desired thermal performance, resulting in reduced space, weight, support structure, footprint, energy requirement and cost. Depending on the application, various types of augmented heat transfer surfaces such as plain fins, wavy fins, offset strip fins, louvered fins and perforated fins are used. They have a high degree of surface compactness and substantial heat transfer enhancement obtained as a result of the periodic starting and development of laminar boundary layers over interrupted channels formed by the fins and their dissipation in the fin wakes. [#ARTNUM](#article-26207-2013946548)
Suppliers
4.2 Finned tube heat exchanger
Finned tube heat exchangers have tubes with extended outer surface area or fins to enhance the heat transfer rate from the additional area of fins. Finned tubes or tubes with extended outer surface area enhance the heat transfer rate by increasing the effective heat transfer area between the tubes and surrounding fluid. There are several types of fins. [Source](https://www.enggcyclopedia.com/2012/03/finned-tube-heat-exchangers/)
Fin and tube heat exchangers are most widely used due to the extended surface for heat transfer in many industrial applications such as waste heat recovery units, heating, ventilation, and air conditioning and refrigeration systems [#ARTNUM](#article-26132-2470079271)
Several designs exist for the fins. New heat exchange tube types with higher performance have been designed, such as the 3-D finned tube, spiral finned tube, serrated finned tube, H-type finned tube, slotted finned tube and so on. [#ARTNUM](#article-26132-2900762659)
4.3 Plate-fin-and-tube heat exchanger
The plate fin-and-tube heat exchangers are widely used in variety of industrial applications, particularly in the heating, airconditioning and refrigeration, HVAC industries. There are many different types of geometry for heat exchangers available. Commonly they are composed of tubes, with plates perpedicular, resulting in a cross flow profile as seen in the figure. There are different types of plate-fin geometry, the most common being the plain fin, where the fins are parallel plates attached to a hot element in the form of tubes or some other shape. These fins act as a sink, absorbing the heat out of the hot element with the help of conductive heat transfer. And then dissipating this absorbed heat onto the outside environment which is at a lower temperature. [#ARTNUM](#article-26206-840680848)
4.4 Corrugated plate heat exchanger
The corrugated plate heat exchanger consists of a number of gasketed plates constrained between an upper carrying bar and a lower guide bar. The plates are compressed between the fixed frame and the movable frame by using many tie bolts. In addition to the plate efficiency, corrugation patterns that produce turbulent flows, it is not only cause's unmatched efficiency; it also produces a heat exchanger self-cleaning nature, which in turn reducing the fouling effect. There are several patterns possible on corrugated plates.
[#ARTNUM](#article-26205-2561023270)
4.5 Coil wired tube heat exchanger
To enhance the mixing in a tube, and therefore improve heat transfer a wired coil helical structure can be added to the tube. [#ARTNUM](#article-26751-2519485646)
4.6 Twisted-tape tube heat exchanger
A twisted tape insert is one of the most efficient heat transfer enhancement methods which has a wide range ofusages due to simplicity, low cost, easy installment and routinemaintenance[79]. Generally, twisted tape performs as a continuous swirl generator which causes turbulence on flow. This leads to a better mixing of the fluid which eventually results in a higher heat transfer rate. [#ARTNUM](#article-26311-2519485646)
4.7 Rotor enhanced shell and tube
In order to improve heat transfer efficiency and solve the fouling problem, a new type heat exchanger whose tube inserted with plastics rotors was designed in the study. [#ARTNUM](#article-26249-2141855446)
4.8 Metal foam heat exchangers
Opencell porous metal foams have received attention for use in compact heat exchangers due to their increasing availability and improved thermal performance. In recent years, considerable research has been conducted on use of metallic and nonmetallic foams to further improve performance of stateoftheart heat exchangers.[#ARTNUM](#article-27304-2070465275). They can be used as an enhancement in plate or tube heat exchangers, as shell-filling material or plate material (see pictures).
**Research findings:**
- In this paper, open-cell aluminum foam is considered as a highly compact replacement for conventional louver fins in brazed aluminum heat exchangers.[#ARTNUM](#article-27304-1996174950)
- The heat exchanger performance is one of the main contributors to the thermodynamic and cost effectiveness of the entire LNG regasification system. Within the paper, the authors discuss a new concept for a compact heat exchanger with a micro-cellular structure medium to minimize volume and mass and to increase thermal efficiency. Numerical calculations have been conducted to design a metal-foam filled plate heat exchanger and a shell-and-tube heat exchanger using published experimental correlations. The results show that the metal-foam plate heat exchanger has the best performance at different channel heights and mass flow rates of fluid. In the optimized configurations, the metal-foam plate heat exchanger has a higher heat transfer rate and lower pressure drop than the shell-and-tube heat exchanger as the mass flow rate of natural gas is increased. [#ARTNUM](#article-27304-2196335867)
5 Regenerative
BackA regenerative heat exchanger, or more commonly a regenerator, is a type of heat exchanger where heat from the hot fluid is intermittently stored in a thermal storage medium before it is transferred to the cold fluid. To accomplish this the hot fluid is brought into contact with the heat storage medium, then the fluid is displaced with the cold fluid, which absorbs the heat.
5.1 Fixed matrix heat exchanger
In a fixed matrix regenerator, a fluid moves through a fixed bed, storing its heat in one direction. When the flow is reversed, another (or the same) fluid can take up this heat again. Phase transitions can also be used.
5.2 Rotary heat exchanger
Rotary heat exchangers or heat wheels are popularly used for heat recovery in many industrial and domestic applications.[#ARTNUM](#article-26250-2790684841). They employ rotary 'heat storing elements' that rotate between cold and hot streams to exchange heat.
The rotor consists of large scale of heat transfer plates known as matrix. The matrix can be made of steel, ceramic, glass and plastic. The rotor rotates continuously with a constant fraction of the core in the flue gas stream and the remaining fraction in the cooling air stream. The saturated wet flue gas is cooled by the matrix, and the water vapor is condensed on the wall of the matrix as the decrease in temperature of flue gas. [#ARTNUM](#article-26250-2902036760)
5.3 Rotating hood regenerator
In a rotating hood regenerating, the heat storage elements are stationary, while the elements trhough which the fluids flow rotate. In principle it is the opposite from a rotary heat exchanger.
**Patent findings:**
Regenerative heat exchanger for heating > =2 parallel air or gas streams consists of a rotating hood over a fixed chamber of solid material for heat retention. The hood is one of a pair above and below the chamber and is divided into >=2 sections either side of a central axis. The flow area of each pair of sections is the same. These radiate from the centre where there are several concentric ducts for the various parallel gas or air streams. The hood and the central ducts are sealed from the hot exhaust gas flowing outside the hood by flexible seals. These are held in position by springs the tension of which can be adjusted. Device is of use in recovering heat from an exhaust gas stream where two or more temp. controlled air streams are required e.g. for preheating prim. and sec. air.[#ARTNUM](#article-26253-2875827312)
5.4 Microscale regenerative heat exchanger
When a hot fluid flows through the cell, heat from the fluid is transferred to the cell wells, and stored there. When the fluid flow reverses direction, heat is transferred from the cell walls back to the fluid. It has a multilayer grating structure in which each layer is offset from the adjacent layer by half a cell which has an opening along both axes perpendicular to the flow axis. Each layer is a composite structure of two sublayers, one of a high thermal conductivity material and another of a low thermal conductivity material.[Wiki](https://en.wikipedia.org/wiki/Regenerative_heat_exchanger)
A micro-scale regenerator has been designed, analytically optimized, and fabricated. The regenerator composed of multiple layers of photoresist-nickel structure in an offset grating pattern. The offset pattern and composite structure minimizes axial conduction losses and disrupts boundary layer formation for improved heat transfer. [#ARTNUM](#article-26764-1997390424)
6 Direct contact
BackDirect contact heat exchangers involve heat transfer between hot and cold streams of two phases in the absence of a separating wall. Thus such heat exchangers can be classified as:
- Gas – liquid
- Immiscible liquid – liquid
- Solid-liquid or solid – gas
Most direct contact heat exchangers fall under the Gas – Liquid category, where heat is transferred between a gas and liquid in the form of drops, films or sprays.
6.1 Gas-solid heat exchangers
Gas-solid heat exchange is facilitated by bed-type heat exchangers, most commonly by solid granules forming a bed.
6.2 Spray column
A spray tower (or spray column or spray chamber) is gas-liquid contactor used to achieve mass and heat transfer between a continuous gas phase (that can contain dispersed solid particles) and a dispersed liquid phase. It consists of an empty cylindrical vessel made of steel or plastic, and nozzles that spray liquid into the vessel. The inlet gas stream usually enters at the bottom of the tower and moves upward, while the liquid is sprayed downward from one or more levels. This flow of inlet gas and liquid in opposite directions is called countercurrent flow.[Wiki](https://en.wikipedia.org/wiki/Spray_tower)
Cooling towers also use a spray-type system
6.3 Tray column
A plate column (or tray column) is a chemical equipment used to carry out unit operations where it is necessary to transfer mass between a liquid phase and a gas phase. In other words, it is a particular gas-liquid contactor. The peculiarity of this gas-liquid contactor is that the gas comes in contact with liquid through different stages; each stage is delimited by two plates (except the stage at the top of the column and the stage at the bottom of the column). [Wiki](https://en.wikipedia.org/wiki/Plate_column)
Different types of tray columns exists, such as disk and donut, sieve trays etc.
6.4 Bubble column
A bubble column reactor is an apparatus used to generate and control gas-liquid chemical reactions. It consists of a vertically-arranged cylindrical column filled with liquid, at the bottom of which gas is inserted. [Wiki](https://en.wikipedia.org/wiki/Bubble_column_reactor)
7 Compact
BackCompact heat exchangers are becoming increasingly important elements in many industrial processes, both in their original role as contributors to increased energy efficiency, and more recently as the basis for novel ‘intensified' unit operations.
7.1 Microchannel heat exchanger
Microchannels (broadly ⩽1 mm) represent the next step in heat exchanger development. They are a particular target of research due to their higher heat transfer and reduced weight as well as their space, energy, and materials savings potential over regular tube counterparts.[#ARTNUM](#article-26150-2083412469). Microchannel heat exchangers can be used for many applications including: high-performance aircraft gas turbine engines, heat pumps and air conditioning.
Microchannel heat exchangers can be produced in the same wat as printed circuits, through etching and diffusion bonding. [#ARTNUM](#article-26150-2475723589)
Machining of thin metal foils with specially contoured diamond cutting tools allows the production of small and very smooth fluid microflow channels for micro heat exchanger applications. Heat exchanger plate wall thickness, as well as fin dimensions, may be carefully controlled and machined to dimensions on the order of tens of micrometers. The plates are stacked and bonded with the vacuum diffusion process to form a crossflow, platetype heat exchanger.[#ARTNUM](#article-26150-2077945856)
7.2 Hollow fiber heat exchanger
Hollow fiber heat exchangers are similar to shell and tube heat exchangers, however they are much more compact and have large surface areas. Usually they are formed using polymers.
**Research findings:**
-Despite polymer materials’ low thermal conductivities (0.1–0.4 W/m K, which is 100–300 times lower than metals), by using hollow polymer fibres with the diameters less than 100 μm, the surface area/volume ratio of polymer hollow fibre heat exchangers can be very high. This makes them extremely efficient with superior thermal performance. [#ARTNUM](#article-26752-2303822880)
7.3 Meso heat exchanger
Meso heat exchangers have a very large surface area density >3000 m2/m3.
**Research findings:**
The current investigation is concerned with the use of a heat exchanger that has a surface area density (β) of 4000 m2/m3 [#ARTNUM](#article-26534-2792620623)
7.4 Microjet heat exchanger
This paper describes the development of heat exchanger with microjet technology, proposed for a waste heat recovery from a range of processes. The article presents a comprehensive study on the heat transfer enhancement in prototype heat exchanger. The heat exchanger is based on multiple jet impingement on the cylindrical heat transfer surface. It comprises four coaxial pipes (a supply channel and a return channel for two fluids). The design of the heat is based on available on the market standardized materials. [#ARTNUM](#article-26216-2571195246) Its essential core is a series of plates. Impinging jets are created by introducing plates with four nozzles of 400 and 600 µm in diameter. The nozzles were created by drilling 1 mm thick plate. These plates are separated by spacers/gaskets made of PTFE. Microjet geometry can be varied by exchanging the nozzle plates and spacers of heat exchanger. [#ARTNUM](#article-26216-2278329116)
7.5 Marbond heat exchanger
The Marbond heat exchanger/reactor family of products is the latest truly innovative design to enter the CHE marketplace. Produced by Chart Marston at their UK factory, an ‘opened up' version of the Marbond unit is shown in Fig. 3 (scale — the unit shown is about the size of a lap-top computer with channels about 1 mm hydraulic diameter). It extends the choice of users who are looking for high integrity, highly compact units able to operate over a range of pressures and temperatures not met with more conventional gasketed or welded CHEs. The manufacturing procedures are similar to those of the PCHE (chemical etching and diffusion bonding), but the construction allows the use of small passageways, which significantly increases the porosity of the heat exchanger core. This can result, in appropriate applications, in a substantially higher area density than the PCHE. For example, a doubling of porosity, other factors being equal, results in a halving of the volume for a given surface area. The design is particularly versatile in terms of the number of passes and number of streams, and the type can be used for a wide variety of duties involving single phase liquids and gases or two phase streams, as well as for reactions. [#ARTNUM](#article-26535-1989674565)
8 Trends
BackThere are some trends in heat exchangers that affect their design or material use.
8.1 3D printed heat exchangers
By 3D printing complex structures can be made, usually of the shell and tube type heat exchangers. Common shapes that are employed are Y-type and H-type tubes, as well as spirals, but the possibilities of 3D-printed heat exchangers are almost limitless. Especially for compact heat exchangers they are interesting.
**Research findings:**
- In the present study, threedimensional (3D) fractaltreelike heat exchangers were designed and manufactured using 3D printing technology.[#ARTNUM](#article-26220-2884496616)
News
8.2 Nano fluids-based
In recent years, adding solid particles to a heat transfer medium has been one of the considerable techniques for increasing heat transfer rate in heat exchangers. Although they have drawn many attentions, they cause some problems such as high pressure drop, abrasion, clogging and sedimentation. But using nanofluids causes a relatively higher increase of heat transfer in comparison to solid particles. In order to tackle above-mentioned problems, nanofluids are used with solid particles which are in very small sizes and low concentrations. [#ARTNUM](#article-26217-2519485646)
Adding nanoparticles to heat exchange fluids improves their thermal conductivity and improves convection. [#ARTNUM](#article-26217-2064293455)
8.3 Polymer heat exchangers
The conventional heat exchanger manufactured in metal (such as stainless steel, copper and aluminium) has the disadvantages in terms of weight and cost. In addition, specially treated metal heat exchangers are needed if the working fluids are corrosive. Given these considerations, it is desirable to find an alternative material for heat exchangers that can overcome these disadvantages and also acquire comparable heat exchange efficiency and be easily fabricated. This is where the use of polymer heat exchanger comes into play. With the advantages of greater fouling and corrosion resistance, greater geometric flexibility and ease of manufacturing, reduced energy of formation and fabrication, and the ability to handle liquids and gases (i.e, single and two-phase duties), polymer heat exchangers have been widely studied and applied in the field of micro-electronic cooling devices, water desalination systems, solar water heating systems, liquid desiccant cooling systems, etc. Most importantly, the use of polymer materials offers substantial weight, space, and volume savings, which makes it more economically competitive compared with exchangers manufactured from many metallic alloys. [#ARTNUM](#article-26457-2303822880)
8.4 Phase change material heat exchange
A phase change material (PCM) is a substance with a high heat of fusion which, melting and solidifying at a certain temperature, is capable of storing and releasing large amounts of energy. Heat is absorbed or released when the material changes from solid to liquid and vice versa; thus, PCMs are classified as latent heat storage (LHS) units. [Wiki](https://en.wikipedia.org/wiki/Phase-change_material)
Phase change materials are commonly studied for storage applications, however they are also interesting for heat exchangers. Art. [#ARTNUM](#article-29666-953775078)
**Research findings:**
- The heat exchanger used in this work is a modular type which is similar to the shell and tube heat exchanger. The shell side is filled with Phase Change Materials (PCM) and air flow is through the tubes in the module. The modules of the heat exchanger are arranged one over other with air spacers in between each module. The air space provided in between the module increases the retention time of the air for better heat transfer. Transient Computational Fluid Dynamics modeling is carried out for single air passage in a modular heat exchanger. It shows that the PCM phase transition time in the module in which different shape of fins is adopted. The module with rectangular fins has 17.2 % reduction in solidification compared with the plain module. Then steady state numerical analysis is accomplished to the whole module having the fin of high heat transfer, so that pressure drop, flow and thermal characteristics across the module and the air spacers are determined for various air inlet velocities of 0.4 to 1.6 m/s. Art. [#ARTNUM](#article-29666-2075619204)
Final Results
Published 09/16/2019
After the midway results meeting, 46 heat exchangers have been reviewed and deepened. The results are organised based on the concept and presented per heat exchanger comprising a description, findings, application (areas), suppliers (if applicable), images, videos, useful links and a reference list. The technology requirements are measured and shown in the [requirements table](#requirements-table). When the heat exchangers were well established in industry the limits (max pressure and temperatures) are given. When this is not the case and specific information was lacking, any values found for that technology were used to give an indication of their applicability range. Capacities of heat exchangers are not easily found, since different sizes are possible as well as parallel systems. By using the concept links below, you can quickly navigate to the concepts and their Heat exchanger descriptions.
Table of concepts:
Technology | Ranking | Capacity | Max (working) Pressure | Max. design temperature (°C) |
---|---|---|---|---|
1.1 Brazed plate heat exchanger (BPHE) |
(
)
|
Single phase 50-100 kW/m²; Two-phase: 1 – 20 kW/m²; up to 30,000 kW cooling capacity | 30-45 Bar (specific go up to 170 bar, depending on metal brazing) | -100 to 200-230 |
1.2 Gasketed plate heat exchanger (GPHE) |
(
)
|
Heating duty 9.6 MW/unit (Hestia) | 16-25 bar (70 bar for specific GPHE) | -25 to 180 and -40 to 200 for special type (depending on gasket) |
1.3 Welded plate heat exchanger (WPHE) |
(
)
|
200 MW condensation output or >1000 m² | 50 bar (up to 100 bar) | 450 (up to 900 in specific types) |
1.4 Spiral plate heat exchangers (SPHE) |
(
)
|
Max heat transfer area of 900 m² and 2500 m² depending on the type | 16 Bar (up to 200) | -100 to 200 (up to 450) |
1.5 Printed circuit heat exchanger (PCHE) |
(
)
|
1,300 m² /m³ and a heating duty up to 1.4 MW | 1000 bar | -200 to 1000 (up to 1500 for special case) |
1.6 Pillow-plate heat exchangers (PPHE) |
(
)
|
Not specified | vacuum to 60-100 bar | 400 (up to 800) |
1.7 Plate and Shell heat exchanger |
(
)
|
2000 m²/unit | 40 bar (up to 200) | -196 to 400 (up to 900) |
1.8 Scraped-surface heat exchangers (SSHE) |
(
)
|
4.5 m²/unit; up to 22000 kg/h | 21 bar (up to 120 possible) | -75 to 250 |
1.9 Wide-gap plate heat exchanger |
(
)
|
Not specified | 15 bar | 180 |
1.10 Capsule-type plate heat exchanger |
(
)
|
N.A. | N.A. | N.A. |
2.1 Shell and Tube Designs (TEMA) |
(
)
|
1 kW - 30MW/unit or 10 to 1000 m² per shell | 400 bar; max. overpressure shell and tube sides 15-40 bar. | 500 (up to 1000) |
2.2 Flat tubes heat exchanger |
(
)
|
Not specified | 20 bar | 200 |
2.3 Twisted tube heat exchanger |
(
)
|
Not specified | Assumed similar to flat tubes/STHE | Assumed similar to flat tubes/STHE |
2.4 Multipass-type heat exchanger |
(
)
|
Not specified | 10 bar | 185 |
2.5 Falling-film heat exchanger |
(
)
|
150 t/hr | Not specified | Not specified |
2.6 Helical baffled heat exchanger |
(
)
|
Assumed similar to STHE | Assumed similar to STHE | Assumed similar to STHE |
2.7 ROD baffled heat exchanger |
(
)
|
Assumed similar to STHE | Assumed similar to STHE | Assumed similar to STHE |
3.1 Double pipe heat exchanger (DPHE) |
(
)
|
0.25 to 200 m² | Usually between 10-50 bar (small units) 310 bar | 300, high temperatures possible |
3.2 Triple concentric tube heat exchanger (TCTHE) |
(
)
|
Not specified | 60 bar | Not specified |
3.3 Helical coil heat exchanger |
(
)
|
Not specified | 16 bar | 203 |
3.4 Spiral wound heat exchanger (SWHE) |
(
)
|
up to 150,000 Nm³/h | 300 bar; up to: Tube-side: 1400 bar; shell-side 300 bar; differential pressure up to 50 bar. | -269 to 650 |
4.1 Plate-fin heat exchanger |
(
)
|
Not specified | Aluminium: 130 bar ; steel: 50 bar | Aluminium: 93; Steel 750; up to 900 |
4.2 Finned tube heat exchanger |
(
)
|
Not specified | 70 bar 130 bar | 900 |
4.3 Plate-fin-and-tube heat exchanger |
(
)
|
Not specified | Assumed similar to other extended HEs | Assumed similar to other extended HEs |
4.4 Corrugated plate heat exchanger |
(
)
|
Not specified | Assumed similar to GPHEs and BPHEs | Assumed similar to GPHEs and BPHEs |
4.5 Coil wired tube heat exchanger |
(
)
|
Not specified | Assumed similar to tubular heat exchangers (usually higher pressure drop) | Assumed similar to tubular heat exchangers |
4.6 Twisted-tape tube heat exchanger |
(
)
|
Not specified | Assumed similar to tubular heat exchangers (usually higher pressure drop) | Assumed similar to tubular heat exchangers |
4.7 Rotor enhanced shell and tube |
(
)
|
N.A. | N.A. | N.A. |
4.8 Metal foam heat exchangers |
(
)
|
Not specified | Pressure drop is mainly affected by foams | 650 |
5.1 Fixed matrix heat exchanger |
(
)
|
High capacity | Pressure difference between the streams should not be large, to prevent equilibration of pressure before switching directions. | Depending on bed material >1400 possible |
5.2 Rotary heat exchanger |
(
)
|
up to 150,000 m³/h | Pressure difference should be small (2000Pa max) between streams and with outside. | Usually low temperature (-30 to 100); up to 600 |
5.3 Rotating hood regenerator |
(
)
|
High capacity | Similar to rotary heat exchanger | Similar to rotary heat exchanger |
5.4 Microscale regenerative heat exchanger |
(
)
|
N.A. | N.A | N.A |
6.1 Gas-solid heat exchangers |
(
)
|
Not specified | Not specified | Depends on material, high temperatures possible (>1000 degreesC) |
6.2 Spray column |
(
)
|
High capacity (up to 200,000 m³/h) | Not specified | Usually up to 400 |
6.3 Tray column |
(
)
|
Medium capacity | 40 bar | Similar to spray column |
6.4 Bubble column |
(
)
|
Similar to tray column | Similar to tray column | Similar to tray column |
7.1 Microchannel heat exchanger |
(
)
|
Not specified | 50 bar | 120 |
7.2 Hollow fiber heat exchanger |
(
)
|
Thermal power 40 kW, flow rate 1000 L/h (prototype) | 10 bar | up to 140 |
7.3 Meso heat exchanger |
(
)
|
N.A. | N.A. | N.A. |
7.4 Microjet heat exchanger |
(
)
|
N.A. | N.A. | N.A. |
7.5 Marbond heat exchanger |
(
)
|
Not specified | up to 400 bar | up to 900 |
8.1 3D printed heat exchangers |
(
)
|
N.A. | N.A. | N.A. |
8.2 Nano fluids-based |
(
)
|
N.A. | N.A. | N.A. |
8.3 Polymer heat exchangers |
(
)
|
Gas flow up to 100,000 Nm³/hr | Low (around 0-10 bar) | Low (<150, but up to 250 in special cases) |
8.4 Phase change material heat exchange |
(
)
|
N.A. | N.A. | N.A. |
1. Plate
BackPlate heat exchangers use the surface of plates (usually stacked) to exchange heat. They are commonly used because of their compactness, ease of production, sensitivity, easy care after set-up and efficiency. Plate type heat exchangers are widely used in process industries for gas/gas applications. Typically, these exchangers prove to be very efficient, especially as air preheaters in process furnaces or in equipment used in environmental protection.
1.1 Brazed plate heat exchanger (BPHE)
A brazed plate heat exchanger (BPHE) is built up from a package of (corrugated) stainless steel plates which are brazed together using materials such as copper and nickel. The plate package is generally sealed by front and rear plate packages to form a self-contained unit. Each plate has a characteristic corrugation pattern that governs the degree of thermal efficiency and hydraulic behavior of the BPHE unit. Four to six apertures are placed in the corners/edges of these plates. Alternate plates are arranged at 180° to each other resulting in the formation of the inlet and outlet port manifolds for the various process fluid circuits. Art. [#ARTNUM](#article-26232-1752739663).
Compactness, low volume, scalability, possibility to achieve close temperature approaches,
relatively high values of the heat transfer coefficients make brazed plate heat exchangers
suitable for a very wide range of applications. They are used especially when corrosion can be an issue since the plates are available in a wide range of materials (copper, copper+, SS brazing materials). In Brazed Plate Heat Exchangers, the brazing process eliminates gasketed joints which allow for higher design pressure and temperatures. [\[Source\]](http://www.graham-mfg.com/gasketed-and-brazed-plate-heat-exchanger-advantages) They can be used with multiple phases.
High turbulent flows at low flow rates can be reached due to the patterns on the plates. This also reduces the fouling within the plates. However, fouling can still occur. The brazed plate heat exchanger is permanently sealed. Due to this backflushing is required for cleaning purposes. Soft debris will be removed, weak acids can be used to enhance the cleaning.
**Applications:** Art. [#ARTNUM](#article-26232-1752739663); [#ARTNUM](#article-26232-2792430176)
* Refridgeration
* Residential heating
* HVAC
* LNG plants
* Dairy/food/beverage industry
1.1.1 | Brazed plate heat exchanger (BPHE) |
---|---|
Brazed plate heat exchanger | |
A brazed plate heat exchanger is characterized by comprising a plurality of heat exchanger sheets and a heat exchanger frame, wherein the heat exchanger frame comprises an end plate and a bottom plate, the heat exchanger sheets are connected with the heat exchanger frame in a brazed mode, a first medium inflow hole is formed in the upper right of the end plate, a first medium outflow hole is formed in the lower left of the bottom plate, a second medium inflow hole is formed in the right lower of the bottom plate, and a second medium outflow hole is formed in the upper right of the bottom plate. After the inlet and outlet direction of the heat exchanger is improved, the flow direction of an industrial low-temperature refrigerating unit provided with the novel heat exchanger is more reasonable; after the improved heat exchanger is used, a heat exchanger pipeline is shorter and simpler. Quite a part of copper pipe materials are saved, heat exchange media flow in copper pipes, and the cost of the whole industrial low-temperature refrigerating unit is reduced. | |
04/15/2015 00:00:00 | |
Link to Article | |
1.1.2 | Brazed plate heat exchanger (BPHE) |
Estimation of Thermal and Hydraulic Characteristics of Compact Brazed Plate Heat Exchangers | |
This thesis work presents various performance estimation methods of compact brazed plate heat exchangers (BPHE) operating in single phase, condenser, evaporator, cascaded and transcritical applications. Such methods play a vital role in development of heat exchanger selection software and during geometry parameter estimation in the new product development process. The suitability of employing commercial computational fluid dynamics (CFD) codes for estimating single phase thermal and hydraulic performance is investigated. Parametric studies are conducted on geometries of single phase fluid sections to isolate and quantify the influence of individual geometric parameters. The influence of mesh characteristics, choice of boundary conditions and turbulent flow modeling on the accuracy of the thermal and hydraulic predictions is presented. Benefits of simulation of fluid flow in entire channels and characteristics of channel flow for different geometric patterns are also presented. A computationally light, general, robust and continuous rating calculation method is developed for implementation in BPHE selection software. The pressure-enthalpy based method provides a generic rating core for various types of applications and provides extensive post processing information of the heat transfer process. General single phase thermal and hydraulic empirical correlations are developed as functions of plate geometric parameters. For facilitating better integration of the developed calculation method with other refrigeration system simulation software, first or higher order continuity is maintained in the sub-routines used for calculating local heat transfer coefficients and refrigerant properties. A new finite grid interpolation method is developed for fast and accurate retrieval of refrigerant properties. The developed method is currently implemented in SSPG7 (BPHE selection software of SWEP International AB) for supporting transcritical CO2 calculations and cascaded heat exchanger calculations. Additionally, the methods developed for single phase and two phase test data evaluation based on meta-heuristic optimization routines is also presented. The application and results of using the developed rating models for various types of calculations is summarized. Other topics such as influence of variable fluid properties on BPHE rating calculations, influence of multi-pass flow arrangement on lumped BPHE rating calculations are briefly presented. | |
01/01/2013 00:00:00 | |
Link to Article | |
1.1.3 | Brazed plate heat exchanger (BPHE) |
Experimental study on CO2 frosting and clogging in a brazed plate heat exchanger for natural gas liquefaction process | |
Abstract The plate-fin heat exchanger (PFHE), which has been widely used in natural gas liquefaction (LNG) industry at present, has some disadvantages such as being sensitive to the impurities in the feed gas, such as water, CO 2 and H 2 S. Compared with the PFHE, the brazed plate heat exchanger (BPHE), which has been applied in some boil off gas (BOG) recycling LNG plants of small to middle size, has simpler inherent structure and higher impurity tolerance. In this study the BPHE is suggested to replace the PFHE to simplify or even omit the massive CO 2 purification equipment for the LNG process. A set of experimental apparatus is designed and constructed to investigate the influence of the CO 2 concentration of the natural gas on solid precipitation inside a typical BPHE meanly by considering the flow resistance throughout the LNG process. The results show that the maximum allowable CO 2 concentration of the natural gas liquefied in the BPHE is two orders of magnitude higher than that in the PFHE under the same condition. In addition, the solid-liquid separation for the CO 2 impurity is studied and the reasonable separating temperature is obtained. The solid CO2 should be separated below 135 K under the pressure of 3 MPa. | |
04/01/2018 00:00:00 | |
Link to Article | |
1.2 Gasketed plate heat exchanger (GPHE)
In Gasketed Plate Heat Exchangers, each heat transfer plate is fitted with an elastomeric gasket, which seals and distributes the process fluids. The heads, normally referred to as channel covers, include connections to permit the entry of the process fluid into the plate pack. [\[Source\]](http://www.graham-mfg.com/gasketed-and-brazed-plate-heat-exchanger-advantages) The plates can easily be removed for cleaning, expansion, or replacing purposes, drastically reducing maintenance costs. Gasketed Plate Heat Exchangers are limited in high fluid temperatures, by the temperature limitations of the gasket. [\[Source\]](https://www.thermaxxjackets.com/plate-and-frame-heat-exchangers-explained/) [\[Hestia GPHE\]](https://www.neimagazine.com/features/featurepossibilities-for-gasketed-plate-heat-exchangers-4633881/)
The GPHE can handle flows rates up to 2000 m³/hr with a duty up to 30000 kW. Suspensions with a concentration of less than 10 mg/L can be handled. Particles size smaller than 0.6 mm however, cause a rapid increase in pressure drop. Often the system is unsuitable for gas two-phase flow.
The main benefit of using GPHE is the ability to easily dismantle the system. This allows for easy cleaning of the system and the flexibility to increase the heater duty of the heat exchanger during usage. Furthermore, the system is normally the most economical if applicable.
**Applications:**
* District heating
* HVAC
* Nuclear power plants
1.2.1 | Gasketed plate heat exchanger (GPHE) |
---|---|
Development of a Plate Heat Exchanger for High-Temperature and High-Pressure | |
A gasketed plate heat exchanger that has a seal pressure of 6.5 MPa or more has been developed. This heat exchanger can be applied to heat exchangers (design temperature: 182°C, design pressure: 3.43 MPa) for the residual heat removal (RHR) systems of boiling water reactors (BWR).Practical use of gasketed plate heat exchangers under the condition of higher temperature and higher pressure has been achieved by developing a high-pressure-retaining plate and frame, as well as a heat- and radiation-resistant gasket. Various element tests related to strength and performance were conducted in the process of this development. A verification test using a prototype heat exchanger was also conducted, and pressure resistance, heat resistance, radiation resistance, endurance against thermal transients, and heat transfer performance have been confirmed.As a result of this development, gasketed plate heat exchangers can be applied for use under the condition of higher temperature and higher pressure, and various effects such as lower system flow, smaller footprint, easier maintenance, and lower cost for weld inspection are expected, compared to conventional shell & tube heat exchangers.Copyright © 2013 by ASME | |
07/29/2013 00:00:00 | |
Link to Article | |
1.2.2 | Gasketed plate heat exchanger (GPHE) |
Experimental Investigation of the Characteristics of a Chevron Type Gasketed- Plate Heat Exchanger | |
In this study, an experimental set-up is designed and constructed to determine the characteristics of an industrial gasketed-plate heat exchanger with chevron plates. Experiments are performed to measure the temperatures and volumetric flow rates at all ports and the pressure drops between inlet and outlet ports at different channel Reynolds numbers (450-5250). A gasketed-plate heat exchanger with different number of plates with city water as the working fluid for both hot and cold sides is utilized. Mass flow rates and inlet temperatures are changed for different cases during experiments. Pressure drop and temperature values are measured close to inlet and outlet ports to minimize the environmental effects. Volumetric flow rates are measured before the heat exchanger where a fully developed regime is obtained. Results are used to develop new correlations for the heat transfer coefficient and the friction factor for pressure drop calculations for the chevron plates tested. Obtained correlations are compared with correlations in literature. | |
01/01/2011 00:00:00 | |
Link to Article | |
1.2.3 | Gasketed plate heat exchanger (GPHE) |
Heat transfer and pressure drop of a gasket-sealed plate heat exchanger depending on operating conditions across hot and cold sides | |
In a gas engine based cogeneration system, heat may be recovered from two parts: Jacket water and exhaust gas. The heat from the jacket water is often recovered using a plate-type heat exchanger, and is used for room heating and/or hot water supply applications. Depending on the operating conditions of an engine and heat recovery system, there may be an imbalance in the flow rate and supply pressure between the engine side and the heat-recovery side of the heat exchanger. This imbalance causes deformation of the plate, which affects heat transfer and pressure drop characteristics. In the present study, the heat transfer and pressure drop inside a heat exchanger were investigated under varying hot-side and cold-side operating conditions. Thermal efficiency of the plate heat exchanger decreases up to 30% with an operating engine load of 50%. A correction factor for the pressure drop correlation is proposed to account for the deformation caused by an imbalance between the two sides of a heat exchanger. | |
05/01/2016 00:00:00 | |
Link to Article | |
1.2.4 | Gasketed plate heat exchanger (GPHE) |
Performance analysis and optimal design of a gasketed plate heat exchanger | |
Heat exchanger is an essential component in complex engineering systems related to energy transformation industrial scenarios. Gasketed plated heat exchanger is an important part of a condensing or evaporating system, food processing industries. The purpose of this study is to investigate heat transfer rate and pressure drop in a gasketed plated heat exchanger. The use of gasketed plate heat exchanger increases the overall heat transfer coefficient of the exchanger. With the equations of the gasketed plated heat exchanger, mathematical modeling is done and the heat transfer coefficient, friction factor and pressure drop calculations are found. After validating the methodology of ANSYS analysis of a heat exchanger, transfer characteristics and pressure drop are established. | |
01/01/2013 00:00:00 | |
Link to Article | |
1.2.5 | Gasketed plate heat exchanger (GPHE) |
Reduction of milk fouling inside gasketed plate heat exchanger using nanocoatings | |
Fouling inside gasketed plate heat exchangers used in milk production has been reduced using nano-composites coatings. An antifouling coating with low surface energy (low wettability) led to a hydrophobic and oleophobic effect. Test facilities were constructed by the Institute of New Materials (INM) and Institute of Environmental Process Engineering (IUV), University of Bremen in Germany for the investigation of milk adhesion and the stability of the coatings on rectangular plates and small cylindrical ducts. A number of coatings and surface treatments were tested. Certain polyurethane-coated plates and tubes formed thinner deposit layer compared to standard uncoated stainless steel plates and tubes. The cleaning time for one coated tube was reduced by 80% compared to the standard stainless steel one. A pilot plant including a milk pasteurizer at LUFA Nord-West in Oldenburg-Germany was used for the thermal treatment of whey protein solutions. Plates coated with different nano-composites as well as electropolished plates were installed in the heating section of the pasteurizer. Significant differences were observed between coated and uncoated plates. The coated plates showed reduced deposit buildup in comparison with the uncoated stainless steel plates. Polyurethane-coated plates exhibited the thinnest deposit layer. Electro-polished plates also reduced deposit buildup in comparison to the standard stainless steel plates and were almost comparable to the coated plates. The time required for cleaning in place (CIP) with the coated plates was reduced by 70% compared to standard stainless steel plates. | |
12/01/2010 00:00:00 | |
Link to Article | |
1.3 Welded plate heat exchanger (WPHE)
Welded plate heat exchangers are similar to Gasketed plate heat exchangers, but instead, the plates are welded together. They are extremely durable and are ideal for transferring fluids with high temperatures or corrosive materials. The plates are all welded together in one block, they, therefore, can’t be fully dismantled and the heating/cooling capacity is fixed. However, they do allow higher pressure and temperature fluids to be used so you’ll find these mostly in heavy industrial, power plants and oil refinery applications. [\[Source\]](https://theengineeringmindset.com/plate-heat-exchanger-applications/)
Can be used for liquid-liquid and biphasic applications. Also for condensation, evaporation, heating, cooling, heat exchange and vacuum conditions. With a condensation output up to 200 MW. Media which contain fibres and solids can also be used in the tube-side, due to the large open flow area. The strong construction of the WPHE makes it able to have pressure differentials of up to 60 bar.
**Applications:** Art. [#ARTNUM](#article-26241-2062888851)
* Chemical industry: coolers/condensers
* Heavy industrial
* Power plants
* Petrochemical
* Oil and gas
* Pharma/food
1.3.1 | Welded plate heat exchanger (WPHE) |
---|---|
A process survey and business potential analysis for the use of large plate heat exchangers in industrial applications | |
The aim of this thesis work was to investigate and evaluate new possible industrial applications for large welded plate heat exchangers, with heat transfer areas of at least 500 m2. The research has been carried out through thermal design of heat exchangers for a total of nine cases. The nine cases are real-life applications for processes covering the petrochemical, oil & gas, power, and refinery industries. Thermal heat exchanger designs were done using Alfa Laval’s in-house heat exchanger design software called Computer Aided Sales (CAS). The welded plate heat exchanger is more compact and lighter than conventional shell and tube heat exchanger, which constitutes the main competition in many applications. The use of welded plate heat exchangers can result in savings in different ways; some examples include less material used, less inventory needed, possibility to use lower quality heat source and potentially better heat recovery. The heat exchanger positions and the possibility to use welded plate heat exchangers were assessed by analyzing the simulated results of the thermal designs together with the limitations of the given case. In total nine cases were evaluated. Four out of the nine cases had heat exchanger positions with potential for using welded plate heat exchangers. Out of these four cases two were power cycles and two were related to producing Liquefied Natural Gas (LNG). Power cycles and LNG processes are both developing markets. Although the market trends are unruly and uncertain, the overall potential for Alfa Laval products is good. From a thermal design point of view both power cycles and LNG are markets that in time could develop potential business for Alfa Laval. | |
01/01/2018 00:00:00 | |
Link to Article | |
1.3.2 | Welded plate heat exchanger (WPHE) |
Impact of plate design on the performance of welded type plate heat exchangers for sorption cycles | |
Numerical and experimental analysis was carried out to examine the heat transfer and pressure drop characteristics of welded type plate heat exchangers for absorption application using Computational Fluid Dynamics (CFD) technique. The simulation results based on CFD are compared with experimental results. A commercial CFD software package (FLUENT) has been used to predict the characteristics of heat transfer, pressure drop and flow distribution within the plate heat exchangers. In this paper, a welded plate heat exchanger with a plate of chevron embossing type was tested by controlling mass flow rate, solution concentration, and inlet/outlet temperatures. The working fluid is H2O/LiBr solution with the LiBr concentration of 54–62% in mass. The numerical simulation examines the internal flow patterns, temperature distribution and the pressure distribution within the channel of the plate heat exchanger. Three plates of embossing types; chevron embossing, elliptic and round, are proposed and simulated in this paper. The simulation results show reasonably good agreement with the experimental results. Also, the numerical results show that the plate with the elliptical shape gives better performance than the plate of the chevron shape from the viewpoints of heat transfer and pressure drop. | |
06/01/2009 00:00:00 | |
Link to Article | |
1.3.3 | Welded plate heat exchanger (WPHE) |
Use of high performance plate heat exchangers in chemical and process industries | |
Abstract At present, plate heat exchangers constantly open up new application fields in the chemical, process, and allied industries due to their numerous advantages. The channel flow between individual plates is characterized by high turbulence induced at low flow velocities. Heat transfer coefficients are generally higher in plate heat exchangers than in conventional shell-and-tube heat exchangers. According to the nature of the process, physical properties of the media, and allowable pressure drops, plates with a variety of patterns are available to adapt the equipment optimally to the specific process conditions. For handling aggressive media the module welded plate heat exchanger was developed. The laser welded modular design keeps the inherent advantages of plate type heat exchanger. It can be disassembled and mechanically cleaned outside the modules. The capacity can also be subsequently modified by changing the number of plates, or the plate patterns can be altered as it can be with the gasketed units. Typical applications of module welded plate heat exchangers in the chemical industry are acid coolers, thermal oil coolers, or condensers for hydrocarbon mixtures. | |
12/01/1999 00:00:00 | |
Link to Article | |
1.4 Spiral plate heat exchangers (SPHE)
A SPHE consists of two sheets that are rolled around a central rod and therefore two separated concentric channels are made. The ends of the channels are sealed through welding. There are two possibilities to seal the sides of the heat exchanger: using bolts and gaskets to fasten the covering sheets to the heat exchanger or welding the covering sheets to the heat exchanger. Art. [#ARTNUM](#article-26228-2342724403)
The main advantage of the SPHE is its highly efficient use of space. This attribute is often leveraged and partially reallocated to gain other improvements in performance, according to well-known tradeoffs in heat exchanger design. (A notable tradeoff is capital cost vs operating cost.) The structure of the SPHE also results in no dead spots and a close temperature approach. A compact SPHE may be used to have a smaller footprint and thus lower all-around capital costs, or an oversized SPHE may be used to have less pressure drop, less pumping energy, higher thermal efficiency, and lower energy costs. Thermal efficiencies up to 2-3 times higher than a conventional shell and tube heat exchanger can be reached.
The SPHE is great against fouling and high viscous or particulate media. This makes the SPHE good for applications such as pasteurization, digester heating, heat recovery, pre-heating, and effluent cooling. For sludge treatment, SPHEs are generally smaller than other types of heat exchangers. [\[Wiki\]](https://en.wikipedia.org/wiki/Heat_exchanger#Helical-coil_heat_exchangers)
The system is great for liquid-liquid and two-phase duties and ideal for vacuum condensation and can be used for steam heater duties. Differential pressures of up to 50 bar are possible. The easy to open design of the SPHE allows for quick and simple cleaning.
**Research findings:**
* The spiral heat exchanger is self-cleaning equipment with low fouling tendencies, easily accessible for inspection or mechanical cleaning and with minimum space requirements. Art. [#ARTNUM](#article-26228-2065526122)
Two-phase application is possible, as well as liquid-liquid. Especially good for fouling liquids.
**Applications:**
* Dairy/food/beverage industry
* Biogas industry
* Wastewater industry
* Pulp and paper industry
* Heavy industry
* Petrochemical industry
* Chemical industry
1.4.1 | Spiral plate heat exchangers (SPHE) |
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An experimental study of spiral-plate heat exchanger for nitrobenzene-water two-phase system | |
This paper presents the results of two-phase (immiscible liquids) heat transfer studies, conducted using a spiral plate heat exchanger. Experimental studies were conducted using hot water as the service fluid. The two-phase system of nitrobenzene-water in different mass fractions and flow rates was studied as a cold process fluid. The two phase heat transfer coefficients were correlated with Reynolds numbers, Prandtl number, and by the following equation Nu = a. (Re) b . (Pr) c . (X) d , adopting an approach available in the literature for the two-phase flows. The data obtained from the experimental study are compared with the theoretical predictions. The predicted coefficients showed a spread of ± 15 % in the laminar range. This new correlation for predicting Nusselt number may be used for practical applications. | |
01/01/2010 00:00:00 | |
Link to Article | |
1.4.2 | Spiral plate heat exchangers (SPHE) |
Analysis of Heat Transfer in Spiral Plate Heat Exchanger Using Experimental and CFD | |
Heat transfer is the key to several processes in industrial application. In a present days maximum efficient heat transfer equipment are in demand due to increasing energy cost. For achieving maximum heat transfer, the engineers are continuously upgrading their knowledge and skills by their past experience. Present work is a skip in the direction of demonstrating the use of the computational technique as a tool to substitute experimental techniques. For this purpose an experimental set up has been designed and developed. Analysis of heat transfer in spiral plate heat exchanger is performed and same Analysis of heat transfer in spiral plate heat exchanger can be done by commercially procurable computational fluid dynamic (CFD) using ANSYS CFX and validated based on this forecasting. Analysis has been carried out in parallel and counter flow with inward and outward direction for achieving maximum possible heat transfer. In this problem of heat transfer involved the condition where Reynolds number again and again varies as the fluid traverses inside the section of flow from inlet to exit, mass flow rate of working fluid is been modified with time. By more and more analysis and experimentation and systematic data degradation leads to the conclusion that the maximum heat transfer rates is obtained in case of the inward parallel flow configuration compared to all other counterparts, which observed to vary with small difference in each section. Furthermore, for the increase heat transfer rate in spiral plate heat exchanger is obtain by cascading system. | |
10/01/2014 00:00:00 | |
Link to Article | |
1.4.3 | Spiral plate heat exchangers (SPHE) |
Design and Construction of a Spiral Heat Exchanger | |
In this article, the performance and applications of a Spiral Plate Heat Exchanger are demonstrated. Also, governing equation of heat transfer phenomena in such heat exchangers is discussed. Regarding the governing equations, a LAB-sized model of this type of heat exchanger was designed and constructed. Galvanized Iron sheets were used as the heat transfer surfaces. Two Galvanized Iron sheets were rolled together around a central core and, as a result, two separated channels were made. Also, a predesign simulation of the heat exchanger was done using the Fluent software to predict the performance of the heat exchanger. First the geometry was made using Gambit software environment then the model was analyzed through Fluent. Because of less fouling, easier cleaning and high heat transfer coefficient, Spiral Heat Exchanger is a good alternative to the other types of heat exchangers, especially when it’s going to handle high fouling flows or highly viscous fluids. Low fouling rate of the heat exchanger, reduces the need of cleaning and therefore the out of service will be decreased. In the constructed heat exchanger, Nusselt number increases as the mass flow rate increases. Average Nusselt number is about 100 that is very good. | |
01/01/2016 00:00:00 | |
Link to Article | |
1.4.4 | Spiral plate heat exchangers (SPHE) |
EXPERIMENTAL AND NUMERICAL STUDIES OF A SPIRAL PLATE HEAT EXCHANGER | |
An experimental and numerical study of heat transfer and flow characteristics of spiral plate heat exchanger was carried out. The effects of geometrical aspects of the spiral plate heat exchanger and fluid properties on the heat transfer characteristics were also studied. Three spiral plate heat exchangers with different plate spacing (4mm, 5mm and 6 mm) were designed, fabricated and tested. Physical models have been experimented for different process fluids and flow conditions. Water is taken as test fluid. The effect of mass flow rate and Reynolds number on heat transfer coefficient has been studied. Correlation has been developed to predict Nusselt numbers. Numerical models have been simulated using CFD software package FLUENT 6.3.26. The numerical Nusselt number have been calculated and compared with that of experimental Nusselt number. | |
01/01/2014 00:00:00 | |
Link to Article | |
1.4.5 | Spiral plate heat exchangers (SPHE) |
The Application of Spiral-plate Heat Exchanger to Industry of Fine Chemicals | |
This article introduces some structural features of spiral-plate heat exchanger and also summarizes the experience of successful application of it into unit operation in the industry of fine chemicals.At last,this article puts forward the ways on how to use the spiral-plate heat exchanger and the advice of improvement in the design of its structure. | |
01/01/2007 00:00:00 | |
Link to Article | |
1.4.6 | Spiral plate heat exchangers (SPHE) |
Use spiral plate exchangers for various applications | |
The refining industry is one of many which today must deal with numerous changes that are being required by federal, state and local environmental agencies. Most environmental projects are simply that--projects that are constructed to satisfy more stringent regulations. They are not undertaken to increase output, refinery performance or margins. On the contrary, they typically result in the opposite. One area of equipment that can be improved is heat exchangers. There has been a large area of advancement in the last 60 years in compact, non-tubular exchangers that can offer many distinct advantages. One of these is finally beginning to be used in refineries after long ago being accepted into oil and gas production and chemical processing. This is the spiral heat exchanger. Most refineries know little or nothing at all about them, let alone their advantages and disadvantages. Their use may help to reduce capital and maintenance costs of many projects that will be implemented. The paper describes the basic design and characteristics of the spiral heat exchanger, crossflow and combination flow configurations, and limitations. Environmental-related uses discussed are desulfurization, NESHAP benzene stripping, vent condensers, and waste water treatment. The nonenvironmental uses discussed are fractionation and catalytic units. | |
05/01/1995 00:00:00 | |
Link to Article | |
1.5 Printed circuit heat exchanger (PCHE)
The PCHE is a plate-type compact heat exchanger and its core is composed of thin plates (of thickness 1.5–3 mm) made of alloys like stainless steel or inconel alloys, with flow channels etched on them by chemical etching process. The etched plates are stacked one over the other and are bonded together using diffusion bonding. These blocks are welded together to construct the core of the PCHE and the headers are connected to the core for external connections. Printed Circuit Heat Exchanger (PCHE) is a widely chosen plate type compact heat exchanger for high-pressure applications. Art. [#ARTNUM](#article-26243-2767695692)
The complete microchannel heat exchangers are highly compact, typically comprising about one-fifth the size and weight of conventional heat exchangers for the same thermal duty and pressure drops. PCHEs can be constructed out of a range of materials, including austenitic stainless steels suitable for design temperatures up to 800°C, and nickel alloys such as Incoloy 800HT suitable for design temperatures more than 900°C. Single units ranging from a few grams up to 100 tonnes have been manufactured. Art. [#ARTNUM](#article-26243-1980144440) High heat fluxes of 13 kW/cm2 are possible, because of the high surface to volume ratios.
The system is immune to the effect of fluid pressure pulsation and fluid low vibration, has an extremely low fluid inventory, the ability to introduce multiple streams in a cross, counter and or co-flow. The system is also capable of handling gases, liquid, and two-phase applications. With a wide range of possible materials to use.
Thus, the field of applications is also very varied, including specialised chemicals processing, and PCHEs are even to be found orbiting the Earth in the International Space Station! Due to the inherent flexibility of the etching process, the basic construction may readily be applied to both a wider range and more complex integration of process unit operations. Chemical reaction, rectification, stripping, mixing, and absorption, as well as boiling and condensation, can be incorporated into compact integrated process modules. Art. [#ARTNUM](#article-26243-1980144440)
**Applications:**
* Marine
* Energy
* Oil and gas
* Petrochemical
* Refridgeration
* Air separation
* Nuclear
1.5.1 | Printed circuit heat exchanger (PCHE) |
---|---|
Diffusion-Welded Microchannel Heat Exchanger for Industrial | |
The goal of next generation reactors is to increase energy efficiency in the production ofelectricity and provide high-temperature heat for industrial processes. The efficient trans-fer of energy for industrial applications depends on the ability to incorporate effectiveheat exchangers between the nuclear heat transport system and the industrial process.The need for efficiency, compactness, and safety challenge the boundaries of existingheat exchanger technology. Various studies have been performed in attempts to updatethe secondary heat exchanger that is downstream of the primary heat exchanger, mostlybecause its performance is strongly tied to the ability to employ more efficient industrialprocesses. Modern compact heat exchangers can provide high compactness, a measureof the ratio of surface area-to-volume of a heat exchange. The microchannel heatexchanger studied here is a plate-type, robust heat exchanger that combines compact-ness, low pressure drop, high effectiveness, and the ability to operate with a very largepressure differential between hot and cold sides. The plates are etched and thereafterjoined by diffusion welding, resulting in extremely strong all-metal heat exchangercores. After bonding, any number of core blocks can be welded together to provide therequired flow capacity. This study explores the microchannel heat exchanger and drawsconclusions about diffusion welding/bonding for joining heat exchanger plates, with bothexperimental and computational modeling, along with existing challenges and gaps.Also, presented is a thermal design method for determining overall design specificationsfor a microchannel printed circuit heat exchanger for both supercritical (24MPa) andsubcritical (17MPa) Rankine power cycles. [DOI: 10.1115/1.4007578]Keywords: heat exchanger, diffusion welding, diffusion bonding, diffusion modeling,printed circuit heat exchanger, process application, thermodynamic modeling | |
01/01/2013 00:00:00 | |
Link to Article | |
1.5.2 | Printed circuit heat exchanger (PCHE) |
Effects of wavy channel configurations on thermal-hydraulic characteristics of Printed Circuit Heat Exchanger (PCHE) | |
Abstract Printed Circuit Heat Exchanger (PCHE) is a widely chosen plate type compact heat exchanger for high pressure applications. The present work mainly focuses on two high pressure applications; firstly, Helium Cooling System (HCS) of Test Blanket Module (TBM) in International Thermonuclear Experimental Reactor (ITER) and secondly, Intermediate Heat exchangers (IHX) in Very High Temperature Reactors (VHTR). In this work, a reduced numerical model for a single banked PCHE core working in He-He counter flow circuit has been numerically modelled and verified against the results available in the literature. The same model is then extended for studying the effect of three wavy-channel configurations viz. triangular, sinusoidal and trapezoidal in a single banked PCHE core made of Alloy-617. The nature of local flow and heat transfer in the periodic channels has been studied by visualizing the vortex core using iso-normalized helicity surfaces. Thereafter, the thermo-hydraulic performances of these models are compared with straight channel PCHEs. Among the various models studied, the trapezoidal PCHE model is found to offer highest heat transfer with the largest pressure drop compared to sinusoidal, triangular and straight channel based PCHE models. A maximum of 41% increase in the heat transfer rate is predicted for the trapezoidal wavy channel compared to the straight channel PCHEs, for the tested operating conditions. For the sinusoidal and triangular wavy-channel PCHE configurations, the corresponding heat transfer advantages are predicted to be 33% and 28% respectively. The optimal thermo-hydraulic performance is also assessed, considering the thermal performance factor (TPF) obtained for all the three channels. The highest values of TPF are predicted for trapezoidal wavy channels (3.5) which is followed by sinusoidal (2.5) and triangular (1.5) wavy channels. | |
03/01/2018 00:00:00 | |
Link to Article | |
1.5.3 | Printed circuit heat exchanger (PCHE) |
Industrial Microchannel Devices: Where Are We Today? | |
Heatric has been involved in the commercial design and manufacturing of “micro/milli” scale heat exchanger core matrices called Printed Circuit Heat Exchangers (PCHEs) since 1985. These core matrices are formed by diffusion bonding together plates into which fluid flow microchannels have (usually) been formed by photo-chemical machining. Complex fluid circuitry is readily implemented with this technique. Diffusion bonding is a ‘solid-state joining’ process creating a bond of parent metal strength and ductility. The complete microchannel heat exchangers are highly compact, typically comprising about one-fifth the size and weight of conventional heat exchangers for the same thermal duty and pressure drops. PCHEs can be constructed out of a range of materials, including austenitic stainless steels suitable for design temperatures up to 800°C, and nickel alloys such as Incoloy 800HT suitable for design temperatures more than 900°C. Single units ranging from a few grams up to 100 tonnes have been manufactured. Currently there are thousands of tons of such microchannel matrix in hundreds of services — many of them arduous duties on offshore oil and gas platforms where the size and weight advantages of microchannel heat exchangers are of obvious benefit. Whilst these matrices are predominantly involved in thermally simple two-fluid heat exchange, albeit at pressures up to 500 bar, PCHEs have also been used for many multi-stream counter-flow heat exchangers. However the field of applications is very varied, including specialised chemicals processing, and PCHEs are even to be found orbiting the Earth in the International Space Station! Due to the inherent flexibility of the etching process, the basic construction may readily be applied to both a wider range, and more complex integration of process unit operations. Chemical reaction, rectification, stripping, mixing, and absorption, as well as boiling and condensation, can be incorporated into compact integrated process modules. Crucially, the resulting degree of compactness has led printed circuit technology to be the enabling technology in certain duties. Techniques for chemical coating onto the surfaces of channels continue to evolve, with applicability both to protective coatings and catalytically active coatings. We will describe a selection of innovative printed circuit technology examples. Alongside the more esoteric, Heatric is actively extending printed circuit technology to adapt to new market opportunities such as nuclear power generation plant and fuel cell systems. These applications perhaps represent two extremes of the both size and process integration, and thus aptly serve to demonstrate the range of industrial use of microchannel devices.Copyright © 2003 by ASME | |
01/01/2003 00:00:00 | |
Link to Article | |
1.5.4 | Printed circuit heat exchanger (PCHE) |
Methodology to develop off-design models of heat exchangers with non-ideal fluids | |
Abstract Supercritical CO 2 (sCO 2 ) closed Brayton cycles are promising heat engines for next-generation thermal power plants since they are efficient, highly scalable, and compatible with a variety of heat sources. A potential application for these cycles is load-following concentrating solar power plants with thermal storage, which will frequently operate at off-design conditions. Accurate and computationally efficient models of the cycle’s heat exchangers and turbomachinery are required to assess and optimise its off-design performance. The printed circuit heat exchangers (PCHEs) used in the sCO 2 closed Brayton cycle are challenging to model since they exhibit non-ideal-gas effects and typically use zigzag channels, for which flow patterns and heat transfer mechanisms are not completely understood. Moreover, heat transfer correlations that capture all effects relevant to a given geometry and flow conditions are often unavailable. We present a methodology to develop accurate and computationally efficient on- and off-design models of heat exchangers that exhibit complex nonlinear behaviours. This methodology involves fitting a 1D discretised heat exchanger model to experimental data using nonlinear least-squares optimisation. Unknown internal heat exchanger geometric parameters are used as fitting parameters. We demonstrate the proposed methodology by developing numerical models for two PCHEs: (1) an sCO 2 –sCO 2 PCHE operating far from CO 2 ’s critical point and (2) an oil–sCO 2 PCHE operating close to CO 2 ’s critical point, where non-ideal fluid property variations are significant. Test data spans heat loads from 6–48% and 15–39% of name-plate duty for heat exchangers (1) and (2) respectively. Across these operating ranges, the maximum and mean heat transfer prediction residuals are 0.91% and 0.36% for heat exchanger (1) and 3.04% and 1.24% for heat exchanger (2). Additionally, we show that good accuracy can be obtained when using only the channel hydraulic diameter as a fitting parameter. Due to their low computational cost and high accuracy, models developed using the proposed methodology are eminently suitable for off-design modelling and optimisation of the sCO 2 closed Brayton cycle and other power cycles or industrial processes where heat exchangers exhibit complex nonlinear behaviour. | |
12/01/2018 00:00:00 | |
Link to Article | |
1.5.5 | Printed circuit heat exchanger (PCHE) |
Recuperators for micro gas turbines: A review | |
Micro gas turbines are a promising technology for distributed power generation because of their compact size, low emissions, low maintenance, low noise, high reliability and multi-fuel capability. Recuperators preheat compressed air by recovering heat from exhaust gas of turbines, thus reducing fuel consumption and improving the system efficiency, typically from 16–20% to ∼30%. A recuperator with high effectiveness and low pressure loss is mandatory for a good performance. This work aims to provide a comprehensive understanding about recuperators, covering fundamental principles (types, material selection and manufacturing), operating characteristics (heat transfer and pressure loss), optimization methods, as well as research hotspots and suggestions. It is revealed that primary-surface recuperator is prior to plate-fin and tubular ones. Ceramic recuperators outperform metallic recuperators in terms of high-temperature mechanical and corrosion properties, being expected to facilitate the overall efficiency approaching 40%. Heat transfer and pressure drop characteristics are crucial for designing a desired recuperator, and more experimental and simulation studies are necessary to obtain accurate empirical correlations for optimizing configurations of heat transfer surfaces with high ratios of Nusselt number to friction factor. Optimization methods are summarized and discussed, considering complicated relationships among pressure loss, heat transfer effectiveness, compactness and cost, and it is noted that multi-objective optimization methods are worthy of attention. Moreover, 3D printing and printed circuit heat exchanger technologies deserve more research on manufacturing of recuperators. Generally, a metallic cost-effective primary-surface recuperator with high effectiveness and low pressure drop is a currently optimal option for a micro gas turbine of an efficiency of ∼30%, while a ceramic recuperator is suggested for a high efficiency micro gas turbine (e.g. 40%). | |
07/01/2017 00:00:00 | |
Link to Article | |
1.6 Pillow-plate heat exchangers (PPHE)
The pillow plate is constructed using a thin sheet of metal spot-welded to the surface of another thicker sheet of metal. The thin plate is welded in a regular pattern of dots or with a serpentine pattern of weld lines. The welding can be done relative cost-effective and the plates used can be made thinner. After welding the enclosed space is pressurised with sufficient force to cause the thin metal to bulge out around the welds, providing a space for heat exchanger liquids to flow, and creating a characteristic appearance of a swelled pillow formed out of metal. There are various types of design possibilities possible. A pillow plate exchanger is commonly used in the dairy industry for cooling milk in large direct-expansion stainless steel bulk tanks. The pillow plate allows for cooling across nearly the entire surface area of the tank, without gaps that would occur between pipes welded to the exterior of the tank. [\[Wiki\]](https://en.wikipedia.org/wiki/Heat_exchanger#Helical-coil_heat_exchangers)
PPHE are a novel heat exchanger type based on wavy pillowlike plate geometry. Typically, they are composed of parallel plates arranged as a stack. In this way, inner channels within the pillow-plates alternate with outer channels between the adjacent plates, and thus, a structure with alternating inner and outer channels are arranged for the heat transfer media. In heat exchanger applications, several pillow-plates are arranged vertically as a stack, parallel to each other, with alternating channels within and between the pillow-plates. The medium inside the pillow-plates is being continuously redirected by the welding point pattern. This leads to thin boundary layers and good heat transfer performance, and hence, to lower the required heat transfer area and lower investment. On the other hand, internal pressure loss also increases, leading to high operating costs for pumps and compressors. Art. [#ARTNUM](#article-26310-2779667980)
Phase-change applications possible, mainly used for its low fouling capabilities. The system has great cleaning possibilities even sometimes possible while running. Making the PPHE ideal for high hygiene applications (food) and heavy fouling processes.
**Applications:**
* Dairy/food/beverage
* Process industry
* Heat storage
* Automotive
* Pharmaceutical
1.6.1 | Pillow-plate heat exchangers (PPHE) |
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A Numerical Study on Turbulent Single-Phase Flow and Heat Transfer in Pillow Plates | |
Pillow-plate heat exchangers (PPHE) represent an innovative heat exchanger design and are a promising alternative to conventional shell-and-tube and plate heat exchangers. However, no reliable design methods for PPHE are available in the open literature. The aim of our work is to close this gap by carrying out a comprehensive study on fluid dynamics and heat transfer in PPHE. In this contribution, the results of a CFD-based investigation of single-phase turbulent fluid flow and heat transfer in pillow plates are presented. The genuine pillow-plate geometry is reproduced using deformation simulations. This method adequately imitates the hydroforming process during the real manufacturing of pillow plates and thus permits an accurate reconstruction of the wavy pillow-plate channels. The generated geometry is then used to carry out CFD simulations for the investigation of fluid flow, pressure loss and heat transfer in pillow plates. The simulation results are successfully validated against experimental measurements performed by our group. Finally, the use of oval welding spots instead of circular ones, as a possibility for improving the thermo-hydraulic performance of pillow-plates, is investigated. | |
01/01/2014 00:00:00 | |
Link to Article | |
1.6.2 | Pillow-plate heat exchangers (PPHE) |
Heat transfer enhancement in pillow-plate heat exchangers with dimpled surfaces: A numerical study | |
Abstract Pillow-plate heat exchangers (PPHE) represent an innovative, fully welded plate-type heat exchanger. They consist of a stack of panels, which are characterized by “pillow-like” surface. The waviness of the channels enhances mixing in the fluid boundary layers, which consequently augments heat transfer. However, PPHE need further optimization in order to compete with corrugated plate heat exchangers with respect to compactness. In this study, a method to enhance heat transfer in PPHE is proposed, based on a surface modification of pillow plates by secondary dimple structures on their primary wavy surface. The new structured surface of the pillow plates promotes stronger near-wall mixing. | |
05/01/2019 00:00:00 | |
Link to Article | |
1.6.3 | Pillow-plate heat exchangers (PPHE) |
Pillow-Plate Heat Exchangers: Fundamental Characteristics | |
Pillow-plate heat exchangers (PPHE) are a novel heat exchanger type based on wavy pillow-like plate geometry. Typically, they are composed of parallel plates arranged as a stack. In this way, inner channels within the pillow-plates alternate with outer channels between the adjacent plates, and thus, a structure with alternating inner and outer channels is arranged for the heat transfer media. This chapter deals with fundamentals of PPHE covering manufacturing, basic design considerations and general application fields. The geometric variability of PPHE is extremely high, while their performance strongly depends on the particular geometric details. Therefore, the relevant parameters characterizing the complex pillow-plate geometry as well as the corresponding methods for their calculation are considered. These parameters include the internal and external heat transfer surface areas, cross-sectional areas and characteristic lengths. Furthermore, the welding spot arrangement is discussed, which is important for the flow pattern and overall thermo-hydraulic performance characteristics. | |
01/01/2018 00:00:00 | |
Link to Article | |
1.7 Plate and Shell heat exchanger
The plate and shell heat exchanger combines the plate heat exchanger with shell and tube heat exchanger technologies. The heart of the heat exchanger contains a fully welded circular plate pack made by pressing and cutting round plates and welding them together. Nozzles carry flow in and out of the plate pack (the 'Plate side' flow path). The fully welded plate pack is assembled into an outer shell that creates a second flow path ( the 'Shell side'). Plate and shell technology offers high heat transfer, high pressure, high operating temperature, and close approach temperature (up to 1 °
C). While also being able to handle large temperature differences between the introduced fluids. In particular, it does completely without gaskets, which provides security against leakage at high pressures and temperatures. [\[Wiki\]](https://en.wikipedia.org/wiki/Heat_exchanger#Plate_and_shell_heat_exchanger) The system is resistant to thermal shocks and thermal and pressure fatigue, making it a good option for temperature fluctuations.
Plate-and-shell exchangers combine the pressure and temperature capabilities of a cylindrical shell with the excellent heat transfer performance of a plate heat exchanger. While being 60-70 % smaller than a traditional shell and tube heat exchanger. The round plates ensure an even distribution of mechanical loads, without the stress concentrations that occur in the corners of rectangular plates.
The system is available in two types of configurations. The bolted and fully welded system, the bolted systems can be opened for cleaning purposes. And the full welded system is used for higher pressure and temperature applications.
Multi-phase applications are possible.
**Applications:**
* HVAC industry
* Marine/offshore industry
* Dairy/food/beverage industry
* Sugar industry
* Biogas industry
* Refrigeration industry
* Pulp and paper industry
* Heavy industry
* Mining industry
* Petrochemical industry
* Chemical industry
* Condensation
* Steam heating
* Oil coolers
* Gas heaters/coolers
1.7.1 | Plate and Shell heat exchanger |
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A Study on the Performance Analysis in the Plate and Shell Heat Exchanger | |
Heat exchangers are called with important devices which have been widely used in industrial fields. Therefore, the design method for a heat exchanger is an important study in the aspect of energy saving. In this study, performance analyses for two types of plate and shell heat exchangers having a corrugated trapezoid shape of a chevron angle with , were executed and compared with experiments. For this study, the operation liquids were adopted with non-phase changing water. In the analysis, method was used for a plate and shell heat exchanger and a program was constructed. Independent variables for a plate and shell heat exchanger are flow rate and inlet temperature. Compared with experimental data, the accuracy of the developed are at the type A and type B in the heat transfer rate, respectively. In the pressure drop, the accuracy of the proposed program for a plate and shell heat exchanger is within and 5% error bounds for the type A and type B, respectively. | |
01/01/2001 00:00:00 | |
Link to Article | |
1.7.2 | Plate and Shell heat exchanger |
Application of the Fully Welded Plate-and-Shell Heat Exchanger for the Reforming Project of the Water Tracing | |
The fully welded plate-and-shell heat exchange maintains the feature of high heat exchanger effectiveness and compact structure of the general plate heat exchanger.It can be used in the circumstances: higher temperature and higher pressure,possessing the economical and high effective features.The example that it was applied for the reforming project of the water tracing in the Petrochemical Plant of Lanzhou Petrochemical Company introduces technologies and construction features and compares the structures and economy with conventional shell-and-tube heat exchanger,suggesting that it can be applied very wide-ranging in the refine oil and petrochemical industry. | |
01/01/2007 00:00:00 | |
Link to Article | |
1.8 Scraped-surface heat exchangers (SSHE)
An SSHE basically consists of a cylindrical rotating shaft (the “rotor”) within a concentric hollow stationary cylinder (the “stator”) so as to form an annular region along which the process fluid is pumped. The stator acts as the heat-transfer surface, and it is normally enclosed within another cylindrical tube which provides a gap through which a heating or cooling service fluid (for example, steam or ammonia) passes. Attached to the rotor are a number of pivoted blades, each of which scrapes the heat-transfer surface, removing processed fluid and hence allowing unprocessed fluid to come closer to the stator. A cut-away schematic of a typical SSHE is shown in the figure.
SSHE are effective for heavily fouling fluids due to constant removal of containment by the rotors. Moreover, highly viscous fluids can also be used, because of the mixing of the rotors, resulting in a distributed temperature. The systems can also be used for cooling crystallization processes as the crystal are removed constantly from the surface.
The usual size of a SSHE is 4-16 m long, the system is able to handle fluids as high as 65 % wt. of solids. In terms of viscosity, it can handle up to 10000 cP. The near plug-flow behaviour of the systems allows for a transition from a batch to a continuous process.
Applications: Art. [#ARTNUM](#article-26537-2014080855)
* Viscous fluids
* Food
* Pharmaceutical
* Chemical
1.8.1 | Scraped-surface heat exchangers (SSHE) |
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Flow of Second Grade Fluid in a Scraped Surface Heat Exchanger | |
Scraped surface heat exchanger (SSHE) is used in industry for the manufacturing of many foodstuff and these foodstuff behave as non-Newtonian material. So in this work we have mathematically modeled flow inside SSHE by taking second grade fluid. In the SSHE, the gaps between the blades and device wall are narrow so lubrication approximations theory (LAT) can be used to study the various flow properties. Steady incompressible isothermal flow of a second grade fluid is considered about a sequence of pivoted scraper blades in a channel in which lower wall is moving and upper wall is stationary. Flow properties, namely velocities, stream functions, flow rates, expressions for pressure, the forces on the blades and walls in different stations of device are investigated. Graphic representation of different flow parameters involved is also incorporated. Practical Application SSHEs are used in the food industry for the preparation of foodstuff to cook, chill or sterilize the various foodstuffs quickly and efficiently. SSHEs are manufactured for extremely viscous foodstuff such as purees, sauces, margarines, james, spread, soups, baby-food, chocolates, mayonnaise, caramel, fudge, ice-cream, and yoghurt, etc. Foodstuff are non-Newtonian in nature as they possess shear thickening, thinning viscoelastic and visco plastic so it is more realistic to study flow inside SSHE by non-Newtonian fluid model. This study provides fruitful insight to study the flow inside SSHE considering the non-Newtonian nature of foodstuff. | |
04/01/2017 00:00:00 | |
Link to Article | |
1.8.2 | Scraped-surface heat exchangers (SSHE) |
Heat and fluid flow in a scraped-surface heat exchanger containing a fluid with temperature-dependent viscosity | |
Scraped-surface heat exchangers (SSHEs) are extensively used in a wide variety of industrial settings where the continuous processing of fluids and fluid-like materials is involved. The steady non-isothermal flow of a Newtonian fluid with temperature-dependent viscosity in a narrow-gap SSHE when a constant temperature difference is imposed across the gap between the rotor and the stator is investigated. The mathematical model is formulated and the exact analytical solutions for the heat and fluid flow of a fluid with a general dependence of viscosity on temperature for a general blade shape are obtained. These solutions are then presented for the specific case of an exponential dependence of viscosity on temperature. Asymptotic methods are employed to investigate the behaviour of the solutions in several special limiting geometries and in the limits of weak and strong thermoviscosity. In particular, in the limit of strong thermoviscosity (i.e., strong heating or cooling and/or strong dependence of viscosity on temperature) the transverse and axial velocities become uniform in the bulk of the flow with boundary layers forming either just below the blade and just below the stationary upper wall or just above the blade and just above the moving lower wall. Results are presented for the most realistic case of a linear blade which illustrate the effect of varying the thermoviscosity of the fluid and the geometry of the SSHE on the flow. | |
12/01/2010 00:00:00 | |
Link to Article | |
1.9 Wide-gap plate heat exchanger
The wide gap heat exchanger is similar to a gasketed heat exchangers, except that one or more of the channels are wider. It has excellent heat transfer and a compact structure with deeper corrugation, therefore, it is especially suitable for heat exchanging between fibrous and viscous materials/fluids and solid particle-containing fluids. Art. [#ARTNUM](#article-26309-2377641195).
The easy opening of the systems allows for cleaning possibilities. The system can results in a higher pressure drop due to the created high turbulence.
**Applications:**
* Biotech and Pharmaceutical
* Chemicals
* Energy and Utilities
* Food and Beverages
* Mining, Minerals and Pigments
* Pulp and Paper
* Water and Waste treatment
Supplier
1.9.1 | Wide-gap plate heat exchanger |
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Application of the Wide Gap Plate Exchanger in the Squeezing Granulator Unit | |
The wide gap plate exchanger was not only of the excellence of high heat transfer effective and compact structure as general plate exchanger,but also had deeper corrugation,therefore,it was especially suitable for heat exchanging between fiber materials,viscous materials and solid particles.Pellet water heat exchanger in polyethylene squeezing granulator unit was taken as an example,whose appliance technologies and construction features was introduced,and was compared with general plate exchanger,it was suggested that it can be extended and applied actively in the same conditions. | |
01/01/2009 00:00:00 | |
Link to Article | |
1.9.2 | Wide-gap plate heat exchanger |
Extra-wide gap pressureproof plate-type heat exchanger | |
The invention relates to an extra-wide gap pressureproof plate-type heat exchanger comprising one or more heat exchanging units (2). When the extra-wide gap pressureproof plate-type heat exchanger comprises a plurality of heat exchanging units (2), included angles less than 180 degrees are formed by shaft lines positioned among the heat exchanging units (2) in a same plane, and each heat exchanging unit (2) comprises a corrugated heat exchanging plate. When the extra-wide gap pressureproof plate-type heat exchanger comprises the plurality of heat exchanging units (2), the heat exchanging units (2) are in in-line arrangement, i.e. the heat exchanging units (2) are arranged in parallel. The extra-wide gap pressureproof plate-type heat exchanger can obtain better turbulent flow effect at low flow rate and meet the requirements of the heat exchange and the cooling of materials in chemical plants and food and beverage industries. | |
06/16/2010 00:00:00 | |
Link to Article | |
1.10 Capsule-type plate heat exchanger
The capsule-type plate heat exchanger is proposed to address high viscosity fluid which has concave and convex ellipsoidal embossing similar to half capsules. Art. [#ARTNUM](#article-26138-2503965242); and has the advantages of low pressure drop and less deposition due to the straight passages in the channels. Art. [#ARTNUM](#article-26138-2914453957)
Phase-change applications possible, low fouling type. It is still under development and is not industrially applied.
1.10.1 | Capsule-type plate heat exchanger |
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Flow patterns and pressure drop of downward two-phase flow in a capsule-type plate heat exchanger | |
Abstract Capsule-type plate heat exchanger has wide industrial applications for its low flow resistance and less deposition and fouling. To broaden its application in phase-change heat transfer processes, the flow behaviors including flow patterns and pressure drop were experimentally studied in a vertical downward transparent capsule-type plate channel. Three main flow regimes are identified, which are film flow, plug flow and churn flow. Flow pattern transition criteria for downward two-phase flow in plate channel have been developed. Liquid block forms when the shear stress on the wavy film interface is much larger than the surface tension, which indicates the transition to plug or churn flow from film flow. And plug flow transits to churn flow when the liquid block is over aerated due to the flow turbulence. The transition boundries proposed for capsule-type plate channel show good agreement with the corresponding boundries of chevron-type plate channels. To predict the friction pressure drop, a new correlation containing the mixture Reynolds number is proposed to describe the law between the Lockhart-Martinelli parameter and liquid two-phase multiplier, which can reflect the effect of mass flux. The comparison of predicted data and experimental results shows good agreement by 82.4% of the data in ±15% error bands. | |
05/01/2019 00:00:00 | |
Link to Article | |
1.10.2 | Capsule-type plate heat exchanger |
Numerical study on heat transfer enhancement in capsule-type plate heat exchangers | |
Abstract The capsule-type plate heat exchanger is proposed to address high viscosity fluid which has concave and convex ellipsoidal embossing similar to half capsules. In this paper, single-phase flow and heat transfer in a capsule-type plate channel are investigated numerically. Owing to the periodicity of the structure of the capsule-type plate channel, the heat transfers between the hot and cold fluid in a unit cell with periodic boundary conditions are modeled. Shear Stress Transport k - ω model is employed for turbulent flow. Streamlines, velocity and local convective heat transfer coefficient are presented for discussions. The heat transfer enhancement is found to be primarily attributed to the vortices, one of which has the unique butterfly-shaped head. The correlations of friction factor and Nusselt number in turbulent flow regime with Reynolds number from 500 to 12,470 are obtained based on the simulation results. Compared with other plate heat exchangers (e.g., chevron-type), the capsule-type plate heat exchanger has big Nusselt number, small friction factor f and a good performance with respect to Nu / f 1/3 . | |
09/01/2016 00:00:00 | |
Link to Article | |
2. Shell and Tube
BackA shell and tube heat exchanger is a class of heat exchanger designs. It is the most common type of heat exchanger in oil refineries and other large chemical processes, and is suited for higher-pressure applications. The shell and tube is very adaptable and flexible, thus can be used for nearly all applicatiosn. As its name implies, this type of heat exchanger consists of a shell (a large pressure vessel) with a bundle of tubes inside it. One fluid runs through the tubes, and another fluid flows over the tubes (through the shell) to transfer heat between the two fluids. The set of tubes is called a tube bundle. [\[Wiki\]](https://en.wikipedia.org/wiki/Shell_and_tube_heat_exchanger)
There are different design elements that can be used in a shell and tube:
* Baffles: Baffles can be used in the shell to break up or split the flow to increase transfer; some specific types are described in the technologies.
* Floating headers: floating headers can be used when thermal expansion is an issue.
* Tube design: specific tube design is described in the technologies.
2.1 Shell and Tube Designs (TEMA)
A shell and tube heat exchanger is a class of heat exchanger designs. It is the most common type of heat exchanger in oil refineries and other large chemical processes and is suited for higher-pressure applications. [\[Wiki\]](https://en.wikipedia.org/wiki/Shell_and_tube_heat_exchanger)
There are different design elements that can be used in a shell and tube, the Tubular Exchanger Manufacturer’s Association (TEMA) has provided standard nomenclature for describing different configurations of common shell & tube heat exchangers, as can be seen in the figure. [\[TEMA source\]](https://www.engineeringpage.com/heat_exchangers/tema.html)
**Design considerations:**
* The fluids with high velocity, fouling tendency, corrosivity, high temperatures or pressures should go on the tube-side.
* The shell side has lower pressure drops and is usually better suited for condensing vapours (except steam)
* With temperature changes higher than 150 °C thermal expansion may be an issue: floating heads can help.
On tube side:
* Cooling water
– The more-fouling, erosive or corrosive fluid
– The less-viscous fluid
– The fluid at a higher pressure
– The hotter fluid
– The smaller volumetric flowrate
**Applications:**
* Process liquid or gas cooling
* Process or refrigerant vapor or steam condensing
* Process liquid, steam or refrigerant evaporation
* Process heat removal and preheating of feed water
* Thermal energy conservation efforts, heat recovery
* Compressor, turbine and engine cooling, oil and jacket water
* Hydraulic and lube oil cooling
**Application Areas:**
* Power Generation
* HVAC
* Marine Applications
* Pulp and Paper
* Refrigeration
* Pharmaceuticals
* Air Processing and Compressor Cooling
* Metals and Mining
* Transport
Links
2.1.1 | Shell and Tube Designs (TEMA) |
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A Review on Experimental Investigation of Shell and Tube Heat Exchanger using Nano-fluids | |
Heat exchangers are most widely used for heat transfer applications in industries. Shell and Tube heat exchanger is one such heat exchanger, provides more area for heat transfer between two fluids in comparison with other type of heat exchanger. Shell and Tube heat exchangers are widely used for liquid-to-liquid heat transfer applications with high density working fluids. This study is focused on use of shell and tube heat exchanger for nano-fluid as a working fluid. A nano-fluid is a mixture of nano sized particles of size up to 100 nm and a base fluid. Typical nanoparticles are made of metals, oxides or carbides, while base fluids may be water, ethylene glycol or oil. The effect of nano-fluid to enhance the heat transfer rate in various heat exchangers is experimentally evaluated recently. The heat transfer enhancement using nano-fluid mainly depends on type of nanoparticles, size of nanoparticles and concentration of nanoparticles in base fluid. This research work deals with experimental investigation of shell and tube heat exchanger with evaluation of convective heat transfer coefficient, overall heat transfer coefficient, exchanger effectiveness. The main objective of this work is to find effects of these parameters on performance of plate heat exchanger with parallel flow arrangement. IndexTerms—heat transfer rate, Shell and tube heat exchanger, Nano-fluid, flow arrangement.. | |
12/01/2015 00:00:00 | |
Link to Article | |
2.1.2 | Shell and Tube Designs (TEMA) |
An overview on thermal and fluid flow characteristics in a plain plate finned and un-finned tube banks heat exchanger | |
The heat exchangers have a widespread use in industrial, transportation as well as domestic applications such as thermal power plants, means of transport, air conditioning and heating systems, electronic equipment and space vehicles. The key objectives of this article are to provide an overview of the published works that are relevant to the tube banks heat exchangers. A review of available and display that the heat transfer and pressure drop characteristics of the heat exchanger rely on many parameters. Such parameters as follows: external fluid velocity, tube configuration (in-line/staggered, series), tubes rows, tube spacing, fin spacing, shape of tubes, etc. The review also shows the finned and un-finned tube configurations heat exchangers. The important correlations for thermofluids in tube banks heat exchangers also discussed. The optimum spacing of tube-to-tube and fin-to-fin with fixed size (i.e., area, volume) with the maximum overall heat conductance (heat transfer rate) were summarized in this review. In addition, the few studies show the effect of tube diameter in a circular shape compared with elliptic tube shape. Overall, the heat transfer coefficient and pressure drop increases with increasing fluid velocity regardless the arrangement and shape of the tube. In the meantime, the other shape of tubes (such as flat or flattened) for finned and un-finned with the optimum design needs more research and investigation due to have lesser air-side pressure drop and improved air-side heat transfer coefficients. They have putted some the significant conclusions from this review. | |
03/01/2015 00:00:00 | |
Link to Article | |
2.1.3 | Shell and Tube Designs (TEMA) |
Constructal design of a shell-and-tube heat exchanger for organic fluid evaporation process | |
Abstract A shell-and-tube heat exchanger for organic fluid evaporation process is investigated in this paper. A complex function considering the heat transfer and fluid flow performances of the shell-and-tube heat exchanger is introduced as the optimization objective. For the fixed total heat transfer area of the heat transfer tubes, structure optimizations of the shell-and-tube heat exchanger are conducted based on constructal theory. The results show that the complex function has its minimum with an optimal external diameter of the heat transfer tube. Compared the performances of the shell-and-tube heat exchanger with initial design, the total heat transfer rate, total pumping power and complex function after optimization are decreased by 7.59%, 70.65% and 11.50%, respectively. It illustrates that the complex function sacrifices a certain heat transfer performance and greatly improves the fluid flow performance, which results in an evident reduction of the complex function. Among the discussed seven working fluids, the R152a has the smallest complex function, and the R236fa has the biggest complex function. The complex function has its double minimum with an optimal mass flow rate of the hot water or an optimal total tube number. These illustrate that the overall performance of the shell-and-tube heat exchanger can be further improved by choosing appropriate working fluid, mass flow rate of the hot water and total tube number. | |
03/01/2019 00:00:00 | |
Link to Article | |
2.1.4 | Shell and Tube Designs (TEMA) |
Designing and application of a shell and tube heat exchanger for nanofluid thermal processing of liquid food products | |
One of the most commonly used types of heat exchangers is the shell and tube heat exchanger. It has been well established that applications of nanofluids in shell and tube heat exchangers are a competitive alternative for common industrial fluids such as hot water. However, conventional applications of nanofluids are restricted to nonfood industries. So, for the first time, this study aimed to design a shell and tube heat exchanger through Kern method for food applications and involving different equations and calculations in detail, to deploy intelligent thermal equipment and PLC section for controlling the performance of shell and tube heat exchanger, and finally, to apply that heat exchanger for two food products, that is, watermelon and tomato juice, in order to survey the extent to which this equipment, by using nanofluids rather than common hot water systems, can improve temperature–time profile of food systems and diminish their energy consumption. Kern method could accurately estimate the number of tubes, tube pitch, baffle spacing, tubes per pass, as well as shell-side, tube-side, and overall heat transfer coefficients while maintaining pressure drops in acceptable ranges. Application of 2 and 4% alumina nanofluids, instead of hot water, decreased thermal processing time of watermelon juice by 24.14 and 51.72%; similarly, these reduction rates were 22.3 and 48.76% for tomato juice processing. Consequently, energy consumption rates of watermelon juice processing dwindled to 24.64 and 48.34% and of tomato juice to 22.3 and 48.76% through deployment of 2 and 4% Al2O3, compared to hot water, respectively. Practical applications Fluids with suspended particles of nanometals or oxidized metals benefit from better heat transfer properties. There is limited research dealing with effects of adding nanoparticles to conventional thermal fluids for fruit juices processing. So, the goal of this research was to introduce nanofluid technology for thermal processing of food products, increasing heat transfer efficiency in shell and tube exchangers by nanofluids and frugality in energy consumption for pasteurization, reducing thermal processing duration and better quality retention of food products. | |
05/01/2018 00:00:00 | |
Link to Article | |
2.1.5 | Shell and Tube Designs (TEMA) |
Liquid-gas heat exchanger for low pressure refrigerant application | |
Liquid-gas heat exchanger has been developed for subcooling-superheating process of vapor compression refrigeration cycle. Refrigeration cycle utilizes low pressure refrigerant, which facilitates in easy piping installation and spill-proof operation. Experimental and numerical studies have been performed in order to quantify and understand thermal-hydraulic behavior of subcooling-superheating (liquid-gas) heat exchanger. As a result of low pressure refrigerant application, low volumetric flow rate in liquid domain can result in dominant natural convection and thus, poor heat exchanging performance. Also, high volumetric flow rate of low pressure gas refrigerant can increase gas side pressure drop. Both phenomenon were observed in conventional shell and tube heat exchanger application and resulted in system COP (Coefficient of Performance) degradation. This paper deals with development of efficient heat exchanger providing high heat transfer, designed for specific application, composed of multiple-fin and microchannel tubes type heat exchanger installed in shell structure. CFD (Computational Fluid Dynamics) methods are used for design optimization; leading toward improved system performance along with size reduction in comparison to shell and tube heat exchanger. | |
04/01/2017 00:00:00 | |
Link to Article | |
2.1.6 | Shell and Tube Designs (TEMA) |
Review on Experimental Analysis and Performance Characteristic of Heat Transfer In Shell and Twisted Tube Heat Exchanger | |
All new heat exchanger applications in oil refining, chemical, petro-chemical, and power generation are accommodated through the use of conventional shell and tube type heat exchangers. The fundamental basis for this statistic is shell and tube technology is a cost effective, proven solution for a wide variety of heat transfer requirements. However, there are limitations associated with the technology which include inefficient usage of shell side pressure drop, dead or low flow zones around the baffles where fouling and corrosion can occur, and flow induced tube vibration, which can ultimately result in equipment failure. This paper presents a recent innovation and development of a new technology, known as Twisted Tube technology, which has been able to overcome the limitations of the conventional technology, and in addition, provide superior overall heat transfer coefficients through tube side enhancement. This paper compares the construction, performance, and economics of Twisted Tube exchangers against conventional designs for copper materials of construction including reactive metals. | |
01/01/2015 00:00:00 | |
Link to Article | |
2.1.7 | Shell and Tube Designs (TEMA) |
Review Paper on Analysis of Heat Transfer in Shell and Tube Type Heat Exchangers | |
A heat exchanger is a device that is used to transfer thermal energy (enthalpy) between two or more fluids, at different temperatures and in thermal contact The tube diameter, tube length, shell types etc. are all standardized and are available only in certain sizes and geometry. And so the design of a shell-and-tube heat exchanger usually involves a trial and error procedure where for a certain combination of the design variables the heat transfer area is calculated and then another combination is tried to check if there is any possibility of reducing the heat transfer area. A primary objective in the Heat Exchanger Design (HED) is the estimation of the minimum heat transfer area required for a given heat duty, as it governs the overall cost of the HE. But there is no concrete objective function that can be expressed explicitly as a function of the design variables and in fact many numbers of discrete combinations of the design variables are possible as is elaborated below. Traditional optimization techniques do not ensure global optimum and also have limited applications. In the recent past, some experts studied on the design, performance analysis and simulation studies on heat exchangers. Modeling is a representation of physical or chemical process by a set of mathematical relationships that adequately describe the significant process behavior. These models are often used for Process design, Safety system analysis and Process control. A steady state model for the outlet temperature of both the cold and hot fluid of a shell and tube heat exchanger will be developed and simulated, which will be verified with the experiments conducted. Based on these observations correlations to find film heat transfer coefficients will be developed during any process of refining of chemical manufacturing. Then these models are simulated on computer software. In this problem of heat transfer involved the condition where different constructional parameters are changed for getting the higher heat transfer rate within the thermal and hydraulic stability. And various models developed according to the change in physical parameters & results are obtained. These models were developed using latest computers tools like ANSYS, Fluent, and MATLAB etc.. The obtained results were also evaluated by comparing the same with the industrial operating exchanger and found satisfactory. | |
09/01/2014 00:00:00 | |
Link to Article | |
2.2 Flat tubes heat exchanger
Flat tube heat exchangers use flat tubes. This can result in better heat transfer, especially when other design elements, like fins or vortex generators, are used. Flat tubes are often used in cooling applications. The system is optimized for poor heat transfer fluids like oils. The flat tube geometry also results in a low-pressure drop.
**Research findings:**
* The heat exchanger element with flat tubes and vortex generators gives nearly twice as much heat transfer and only half as much pressure loss as the corresponding heat exchanger element with round tubes. Art. [#ARTNUM](#article-26308-1994346551)
Supplier
2.2.1 | Flat tubes heat exchanger |
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Heat Transfer and Pressure Drop Under Dry and Humid Conditions in Flat-Tube Heat Exchangers With Plain Fins | |
Flat-tube heat exchangers could be an interesting alternative to make indirect cooling of display cabinets more energy-efficient. This application involves low air velocities in combination with condensation of water vapor on the air side, so plain fins could be suitable. Two different heat exchangers having flat tubes and plain fins on the air side were evaluated experimentally. One of the heat exchangers had continuous plate fins, and the other had serpentine fins. The performances during dry and wet test conditions were compared and related to theoretical predictions for different assumptions. The influence of air velocity, air humidity, and inclination angle was investigated. The results show that, in most cases, the heat transfer performance is somewhat reduced under wet conditions in comparison with dry test conditions, and that wet heat transfer surfaces lead to an increased pressure drop. At the lower air velocity range that was investigated, the heat exchanger having continuous plate fins drained better than the one with serpentine fins. | |
03/01/2010 00:00:00 | |
Link to Article | |
2.2.2 | Flat tubes heat exchanger |
Local heat transfer and flow losses in fin-and-tube heat exchangers with vortex generators: A comparison of round and flat tubes | |
Abstract Local heat transer on the plate fin of a fin-and-tube heat exchanger element with flat tubes in staggerred arrangement was measured by liquid crystal thermography in the Reynolds number range of 600–3000. The flow loss was estimated from the measure pressure loss. The influence of longitudinal vortex generators on fin heat transfer and floww losses was investigated. The results were compared with similar experimental results for round tubes. For the straggered fin-and-tube arrangement, the longitudinal vorices increase heat transfer only marginally (10%) for round tubes but dramatically (100%) for flat tubes. The heat exchanger element with flat tubes and vortex generators gives nearly twice as much heat transfer and only half as much pressure loss as the corresponding heat exchanger element with round tubes. | |
08/01/1993 00:00:00 | |
Link to Article | |
2.2.3 | Flat tubes heat exchanger |
Performance evaluation analysis of metal foam and flat tube heat exchangers for HVAC applications | |
One of the most commonly used heat exchangers in residential air conditioning applications for heat exchange between air and refrigerant are of the round tube and fin type. Another heat exchanger combines the round tubes with open cell metal foam in the place of the fins. Previous screening studies have shown that combining the metal foam with flat tubes is also a promising possibility. In this work a comparison is made between commonly used louvered fin and round tube heat exchangers and metal foam enhanced flat tube heat exchangers. The comparison is made using computational fluid dynamics (CFD) and a two-dimensional volume averaged model for the metal foam. The influence of the contact resistance, pore density, external porosity, tube spacing and tube width are investigated. It is revealed that the optimum foam height is the minimum value which was considered. | |
05/27/2016 00:00:00 | |
Link to Article | |
2.2.4 | Flat tubes heat exchanger |
Shell-and-tube exhaust-heat boiler with spiral flat tube | |
The utility model discloses a shell-and-tube exhaust-heat boiler with a spiral flat tube. The boiler comprises a shell, wherein the shell is provided with a smoke inlet, a smoke outlet, a water inlet, a steam outlet and an outer head cover; a front end channel box, a fixed tube sheet, a baffle plate, a floating tube sheet and a floating head cover are arranged in the shell; and a spiral flat tube bundle which can allow fluid inside and outside the tube to generate turbulent flow and increase a heat exchange surface is fixedly connected between the fixed tube sheet and the floating tube sheet. The shell-and-tube exhaust-heat boiler with the spiral flat tube of the utility model has the advantages of high heat utilization ratio, compact structure, small size, convenient hosting, material saving, low manufacturing cost and wide application to industries such as petrochemical industry, electric power, steel and iron, nonferrous metals, cement, building materials, light industry, coal and the like. | |
01/12/2011 00:00:00 | |
Link to Article | |
2.2.5 | Flat tubes heat exchanger |
Thermal and Fluid Dynamic Analysis of Compact Fin-and-Tube Heat Exchangers for Automotive Applications | |
Flat tubes heat exchangers are commonly used in many industrial applications as a consequence of the distinctive geometrical characteristics of the flat tube compared with round tube. This paper aims to investigate the flow and heat transfer characteristics of laminar cross-flow forced convection in compact fin-and-flat tube heat exchangers. The experiment was performed to explore the influence of the tube inclination angle on the thermal hydraulic performance of the flat tube heat exchanger. Four flat tubes arranged in two aligned rows having the same longitudinal and transverse pitches have been examined in the range of Reynolds number between 1768.27 and 2259.46. A constant heat flux of 4169.63 W/m2 was applied at the inner surface of each flat tube. On the other hand, the numerical simulation is solved by ANSYS FLUENT for a two dimensional model with unstructured mesh and the results are compared against the experimental results. The numerical simulation results indicate that the average Nusselt number increased by 78.24 % for Reynolds number 1768.27. Besides that, for Reynolds number 1964.75 and 2259.46 the Nusselt numbers were increased by 75.89 % and 54.49%, respectively, compared to experimental results. Moreover, the pressure drop is increased 25 % and 83.38 % for both experimental and numerical simulation with respect to three Reynolds number. It was found that, the tube with 30° degree provides the higher heat transfer with Reynolds number 2259.46. This study could assist engineers in decisions regarding the application of compact fin-and-tube heat exchangers in the automotive field. | |
01/01/2018 00:00:00 | |
Link to Article | |
2.3 Twisted tube heat exchanger
A twisted (oval) tube heat exchanger is a type of heat exchanger that aims at improving the heat transfer coefficient of the tube side and also decreasing the pressure drop of the shell side. Tubes that play an important role in this heat transfer enhancement technique are made from normal round tubes. They are formed into an oval section with a superimposed twist by some special techniques. Two ends of the tubes remain round on the consideration of assembling them with the tube sheet. [#ARTNUM](#article-26126-2049240625)
The tube geometry is a self-supporting structure which eliminates the requirements of baffles. The lack of baffles provides a longitudinal flow pattern. This flow eliminates damage-inducing vibration in the shell, the creation of dead spots and a lower pressure drop.
The twisted tube configuration can have up to 40% more heat transfer area than the traditional shell and tube HEX of the same volume. The twist of the tubes results in a swirl flow around the tube side. This increases the shear velocity and thus decreasing the fluid boundary layer around the tubes, resulting in an enhanced heat transfer.
Bundles in the centre of the shell can be cleaned by a triangular pitch which allows the cleaning of multiple lanes. The shell side can be hydro blasted and chemical cleaning can be used effectively due to the uniform flow pattern.
**Research findings:**
* The analyzing result shows that the twisted oval tube heat exchangers are preferred to work at low tube side flow rate and high shell-side flow rate. Art. [#ARTNUM](#article-26126-2049240625)
Fouling is inhibited compared to conventional STHE; heat transfer enhanced.
**Applications:**
* Petrochemical
* Refining
* Offshore O&G
* Chemical
* Pulp/paper
* Mining/ Minerals
* Crude preheat; Feed/effluent for reformer (CCR and semi-regeneration); Hydrotreater; Hydrocracker; Alkylation; Overhead condensers; Reboilers (kettle and J-Shell); Lean/rich amine; Compressor interstage coolers; Texas Towers; Hydrotreating/Reforming; KBR Rose Exchangers.
2.3.1 | Twisted tube heat exchanger |
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3D numerical simulation on the shell side heat transfer and pressure drop performances of twisted oval tube heat exchanger | |
Abstract Twisted oval tube heat exchanger has been widely used in chemical industry field. In the present study, fluid flow and heat transfer characteristics in the shell side of this type of heat exchanger are studied numerically with Realized k – e model. Influence of the geometrical parameters including twisted pitch length P and aspect ratio A / B on the performance of the shell side are analyzed. Results reflect that Nusselt number and friction factor both increase with the increasing of P and A / B . Their influence on the shell side overall heat transfer performance h /Δ P is also analyzed. It is concluded that the overall heat transfer performance of the shell side increase with the increasing of A / B . But on the aspect of the influence of P , it firstly increases with the increasing of P and then decreases with the increasing of P . Velocity and temperature distributions, stream traces and secondary flow distributions are presented to make the fluid flow and heat transfer characteristics in the shell side clear at the end of the present work. The magnitudes of the total velocity at the self-supporting points are found to be lower and the temperatures are found to be higher than their neighborhoods. Spiral flow can be found in the shell side especially for the cases with A = 14 mm, B = 5 mm. The intensity of the spiral flow becomes more and more drastic with the increasing of A/B and the decreasing of P . Analysis of the secondary shows that the magnitude of the secondary flow increases with the increasing of A/B and decreases with the increasing of P . Irregular secondary flow can also be found around the helixes which are formed by the twisting of the oval sections. | |
10/01/2013 00:00:00 | |
Link to Article | |
2.3.2 | Twisted tube heat exchanger |
Experimental and numerical study of convective heat transfer and fluid flow in twisted oval tubes | |
Abstract Twisted oval tube heat exchanger is a type of heat exchanger aims at decreasing the pressure drop of the shell side. In the present study, heat transfer and pressure drop performances of twisted oval tube have been studied experimentally and numerically. The experimental study of the twisted oval tube shows that heat transfer process can be enhanced but also with an increasing of pressure drop when compared with the smooth round tube. The effects of geometrical parameters on the performance of the twisted oval tube have been analyzed numerically. The result reveals that the heat transfer coefficient and friction factor both increase with the increasing of axis ratio a/b , while both decrease with the increasing of twist pitch length P . The influence of a/b and P on the overall performance of the twisted oval tubes are also studied. Aiming at obtaining the heat transfer enhancement mechanism of the twisted oval tube, secondary flow, total velocity and temperature distributions of flow section are given. From the analysis it can be concluded that the emergence of twist in the twisted oval tube results in secondary flow. It exists in the form of spiral flow when a/b is big, but in the form of up and down when a/b is small. It is this secondary flow that changes the total velocity and temperature distributions of the twisted oval tube when compared with a smooth oval tube with the same sectional geometric parameters. Then the synergy angle between velocity vector and temperature gradient is reduced and the heat transfer process is enhanced. | |
08/01/2012 00:00:00 | |
Link to Article | |
2.3.3 | Twisted tube heat exchanger |
Heat transfer and pressure drop performance of twisted oval tube heat exchanger | |
Twisted oval tube heat exchanger is a type of heat exchanger that aims at improving the heat transfer coefficient of the tube side and also decreasing the pressure drop of the shell side. In the present work, tube side and shell side heat transfer and pressure drop performances of a twisted oval tube heat exchanger has been experimentally studied. The tube side study shows that the tube side heat transfer coefficient and pressure drop in a twisted oval tube are both higher than in a smooth round tube. The shell side study shows that the lower the modified Froude number FrM, the higher the shell side heat transfer coefficient and pressure drop. In order to comparatively analyze its shell side performance of the heat exchanger, a rod baffle heat exchanger with similar size of the twisted oval tube heat exchanger is designed and its performance is calculated with Gentry's method. The comparative study shows that the heat transfer coefficient of the twisted oval tube heat exchanger is higher and the pressure drop is lower than the rod baffle heat exchanger. In order to evaluate the overall performance of the twisted oval tube heat exchanger, a performance evaluation criterion considering both the tube side and shell side performance of a heat exchanger is proposed and applied. The analyze of the overall performance of the twisted oval tube shows that the twisted oval tube heat exchangers works more effective at low tube side flow rate and high shell side flow rate. | |
01/01/2013 00:00:00 | |
Link to Article | |
2.3.4 | Twisted tube heat exchanger |
Heat transfer measurement in a three-phase spray column direct contact heat exchanger for utilisation in energy recovery from low-grade sources | |
Abstract Energy recovery from low-grade energy resources requires an efficient thermal conversion system to be economically viable. The use of a liquid-liquid-vapour direct contact heat exchanger in such processes could be suitable due to their high thermal efficiency and low cost in comparison to a surface type heat exchanger. In this paper, the local volumetric heat transfer coefficient ( U v ) and the active height ( H v ) of a spray column three-phase direct contact heat exchanger (evaporator) have been investigated experimentally. The heat exchanger comprised a cylindrical Perspex tube of 100 cm height and 10 cm diameter. Liquid pentane at its saturation temperature and warm water at 45 °C were used as the dispersed phase and the continuous phase respectively. Three different dispersed phase flow rates (10, 15 and 20 L/h) and four different continuous phase flow rates (10, 20, 30 and 40 L/h) were used throughout the experiments. In addition, three different sparger configurations (7, 19 and 36 nozzles) with two different nozzle diameters (1 and 1.25 mm) were tested. The results showed that the local volumetric heat transfer coefficient ( U v ) along the column decreases with height. An increase in both the continuous and dispersed phase flow rates had a positive effect on U v , while an increase in the number of nozzles in the sparger caused U v to decrease. The active height was significantly affected by the dispersed and continuous phase flow rates, the sparger configuration and the temperature driving force in terms of the Jacob number. | |
10/01/2016 00:00:00 | |
Link to Article | |
2.3.5 | Twisted tube heat exchanger |
Research on Heat Transfer Enhancement of Shutter Baffle Heat Exchanger | |
A new concept of “Sideling Flow” in shell side of shell-and-tube heat exchanger is presented, which is relative to the cross flow, longitudinal flow and helical flow in heat exchanger. A type of new energy saving shell-and-tube heat exchanger with sideling flow in shell side, shutter baffle heat exchanger is invented, which exhibits the significant heat transfer enhancement and flow resistance reducement performance. The “Field Synergy Principle” is adopted to analyze the heat transfer enhancement mechanism of sideling flow, it is indicated that the shutter baffle heat exchanger exhibits the perfect cooperativity between velocity field and temperature grads field. Effects of the structure and processing parameters on the fluid flow and heat transfer are also investigated through numerical simulation, both the correlative equations of heat transfer coefficient and pressure drop in shell side are deduced, which provide references for the design and popularization of this new type heat exchanger. | |
05/01/2011 00:00:00 | |
Link to Article | |
2.3.6 | Twisted tube heat exchanger |
Review on Experimental Analysis and Performance Characteristic of Heat Transfer In Shell and Twisted Tube Heat Exchanger | |
All new heat exchanger applications in oil refining, chemical, petro-chemical, and power generation are accommodated through the use of conventional shell and tube type heat exchangers. The fundamental basis for this statistic is shell and tube technology is a cost effective, proven solution for a wide variety of heat transfer requirements. However, there are limitations associated with the technology which include inefficient usage of shell side pressure drop, dead or low flow zones around the baffles where fouling and corrosion can occur, and flow induced tube vibration, which can ultimately result in equipment failure. This paper presents a recent innovation and development of a new technology, known as Twisted Tube technology, which has been able to overcome the limitations of the conventional technology, and in addition, provide superior overall heat transfer coefficients through tube side enhancement. This paper compares the construction, performance, and economics of Twisted Tube exchangers against conventional designs for copper materials of construction including reactive metals. | |
01/01/2015 00:00:00 | |
Link to Article | |
2.4 Multipass-type heat exchanger
In a multipass type heat exchanger, one fluid moves through the shell multiple times, usually through the use of U-tubes. Multiple-pass shell-and-tube heat exchangers allow thermal expansion and easy mechanical cleaning, as well as longer flow paths for a given exchanger length. In addition, the high velocities achieved for the tube fluid help increase heat transfer coefficients and reduce surface fouling. Art. [#ARTNUM](#article-26148-1985475579)
Using multipass systems gives more flexibility in optimising fluid velocity, pressure drop and heat transfer. A multipass is required if the outlet temperature of the hot stream is below the outlet temperature of the cold stream (temperature cross).
**Applications:**
* Industrial waste heat recovery solutions
* Energy
* Oil and gas industry
* Chemical industry
* Food
* Processes of heating, evaporation, condensation or cooling of products such as oils, effluents, sewage, wastewater, biogas, asphalts, hydrocarbons, exhaust gases, biodiesel, methanol.
2.4.1 | Multipass-type heat exchanger |
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Design and optimization of multipass heat exchangers | |
Abstract In this paper, a simple algorithm is developed for the design and economic optimization of multiple-pass 1–2 shell-and-tube heat exchangers in series. The design model is formulated using the F T design method and inequality constraints that ensure feasible and practical heat exchangers. Simple expressions are obtained for the minimum real (non-integer) number of 1–2 shells in series. A graphical method is also presented to develop some insight into the nature of the optimization problem. The proposed algorithm enables engineers to design optimum multipass heat exchangers quickly and easily. It is also shown how the method can be applied for optimal design of multipass process utility exchangers. | |
05/01/2008 00:00:00 | |
Link to Article | |
2.4.2 | Multipass-type heat exchanger |
Fundamentals of Heat Exchanger Design | |
Preface. Nomenclature. 1 Classification of Heat Exchangers. 1.1 Introduction. 1.2 Classification According to Transfer Processes. 1.3 Classification According to Number of Fluids. 1.4 Classification According to Surface Compactness. 1.5 Classification According to Construction Features. 1.6 Classification According to Flow Arrangements. 1.7 Classification According to Heat Transfer Mechanisms. Summary. References. Review Questions. 2 Overview of Heat Exchanger Design Methodology. 2.1 Heat Exchanger Design Methodology. 2.2 Interactions Among Design Considerations. Summary. References. Review Questions. Problems. 3 Basic Thermal Design Theory for Recuperators. 3.1 Formal Analogy between Thermal and Electrical Entities. 3.2 Heat Exchanger Variables and Thermal Circuit. 3.3 The ?(Epsilon)-NTU Method. 3.4 Effectiveness - Number of Transfer Unit Relationships. 3.5 The P-NTU Method. 3.6 P-N TU R elat ionships. 3.7 The Mean Temperature Difference Method. 3.8 F Factors for Various Flow Arrangements. 3.9 Comparison of the ?(Epsilon)-NTU, P-NTU, and MTD Methods. 3.10 The ?(Psi)-P and P1-P2 Methods. 3.11 Solution Methods for Determining Exchanger Effectiveness. 3.12 Heat Exchanger Design Problems. Summary. References. Review Questions. Problems. 4 Additional Considerations for Thermal Design of Recuperators. 4.1 Longitudinal Wall Heat Conduction Effects. 4.2 Nonuniform Overall Heat Transfer Coefficients. 4.3 Additional Considerations for Extended Surface Exchangers. 4.4 Additional Considerations for Shell-and-Tube Exchangers. Summary. References. Review Questions. Problems. 5 Thermal Design Theory for Regenerators. 5.1 Heat Transfer Analysis. 5.2 The ?(Epsilon)-NTUo Method. 5.3 The ?(Lambda)-?(Pi) Method. 5.4 Influence of Longitudinal Wall Heat Conduction. 5.5 Influence of Transverse Wall Heat Conduction. 5.6 Influence of Pressure and Carryover Leakages. 5.7 Influence of Matrix Material, Size, and Arrangement. Summary. References. Review Questions. Problems. 6 Heat Exchanger Pressure Drop Analysis. 6.1 Introduction. 6.2 Extended Surface Heat Exchanger Pressure Drop. 6.3 Regenerator Pressure Drop. 6.4 Tubular Heat Exchanger Pressure Drop. 6.5 Plate Heat Exchanger Pressure Drop. 6.6 Pressure Drop Associated with Fluid Distribution Elements. 6.7 Pressure Drop Presentation. 6.8 Pressure Drop Dependence on Geometry and Fluid Properties. Summary. References. Review Questions. Problems. 7 Surface Basic Heat Transfer and Flow Friction Characteristics. 7.1 Basic Concepts. 7.2 Dimensionless Groups. 7.3 Experimental Techniques for Determining Surface Characteristics. 7.4 Analytical and Semiempirical Heat Transfer and Friction Factor Correlations for Simple Geometries. 7.5 Experimental Heat Transfer and Friction Factor Correlations for Complex Geometries. 7.6 Influence of Temperature-Dependent Fluid Properties. 7.7 Influence of Superimposed Free Convection. 7.8 Influence of Superimposed Radiation. Summary. References. Review Questions. Problems. 8 Heat Exchanger Surface Geometrical Characteristics. 8.1 Tubular Heat Exchangers. 8.2 Tube-Fin Heat Exchangers. 8.3 Plate-Fin Heat Exchangers. 8.4 Regenerators with Continuous Cylindrical Passages. 8.5 Shell-and-Tube Exchangers with Segmental Baffles. 8.6 Gasketed Plate Heat Exchangers. Summary. References. Review Questions. 9 Heat Exchanger Design Procedures. 9.1 Fluid Mean Temperatures. 9.2 Plate-Fin Heat Exchangers. 9.3 Tube-Fin Heat Exchangers. 9.3.4 Core Mass Velocity Equation. 9.4 Plate Heat Exchangers. 9.5 Shell-and-Tube Heat Exchangers. 9.6 Heat Exchanger Optimization. Summary. References. Review Questions. Problems. 10 Selection of Heat Exchangers and Their Components. 10.1 Selection Criteria Based on Operating Parameters. 10.2 General Selection Guidelines for Major Exchanger Types. 10.3 Some Quantitative Considerations. Summary. References. Review Questions. Problems. 11 Thermodynamic Modeling and Analysis. 11.1 Introduction. 11.2 Modeling a Heat Exchanger Based on the First Law of Thermodynamics. 11.3 Irreversibilities in Heat Exchangers. 11.4 Thermodynamic Irreversibility and Temperature Cross Phenomena. 11.5 A Heuristic Approach to an Assessment of Heat Exchanger Effectiveness. 11.6 Energy, Exergy, and Cost Balances in the Analysis and Optimization of Heat Exchangers. 11.7 Performance Evaluation Criteria Based on the Second Law of Thermodynamics. Summary. References. Review Questions. Problems. 12 Flow Maldistribution and Header Design. 12.1 Geometry-Induced Flow Maldistribution. 12.2 Operating Condition-Induced Flow Maldistribution. 12.3 Mitigation of Flow Maldistribution. 12.4 Header and Manifold Design. Summary. References. Review Questions. Problems. 13 Fouling and Corrosion. 13.1 Fouling and its Effect on Exchanger Heat Transfer and Pressure Drop. 13.2 Phenomenological Considerations of Fouling. 13.3 Fouling Resistance Design Approach. 13.4 Prevention and Mitigation of Fouling. 13.5 Corrosion in Heat Exchangers. Summary. References. Review Questions. Problems. Appendix A: Thermophysical Properties. Appendix B: ?(Epsilon)-NTU Relationships for Liquid-Coupled Exchangers. Appendix C: Two-Phase Heat Transfer and Pressure Drop Correlations. C.1 Two-Phase Pressure Drop Correlations. C.2 Heat Transfer Correlations for Condensation. C.3 Heat Transfer Correlations for Boiling. Appendix D: U and CUA Values for Various Heat Exchangers. General References on or Related to Heat Exchangers. Index. | |
01/01/2003 00:00:00 | |
Link to Article | |
2.4.3 | Multipass-type heat exchanger |
Numerical Simulation of U-tube Heat Exchanger Inlet Section Flow Field | |
The three-dimensional steady flow mathematical model about inlet section of U tube type heat exchanger was established, and then the pressure field distribution, temperature field distribution and velocity field distribution of the U type heat exchanger were obtained by the model. Based on this, the pressure field, temperature field and velocity field of the U type heat exchanger were discussed. The results show that, increasing inlet velocity of hot fluid in the U type heat exchanger, for one thing,can increase heat exchange; for another, the longer the running time, the lower the internal temperature of the heat exchanger,the higher the outlet velocity, the lower the total heat transfer rate, the pressure loss first decreases and then tends to stability; corrosion erosion effect in all regions of U type heat exchanger is enhanced, especially the area between the U type heat exchanger inlet and the casing wall. | |
01/01/2014 00:00:00 | |
Link to Article | |
2.5 Falling-film heat exchanger
A falling-film heat exchanger is characterized by one fluid forming a film on the inside of a tube while being cooled or heated from the shell side. Usually, the film is facilitated by gravity (vertically), although other types do exist. The created film results in a short residence time with a high evaporation rate. It is essential that the whole column stays wetted during operation.
It is often used as an evaporator in industry, to concentrate solutions. [\[Wiki\]](https://en.wikipedia.org/wiki/Falling_film_evaporator)
The capacity of a falling-film heat exchanger is 150 ton/hr with a possible heat transfer area of 0.3-4800 m². The heat exchanger is suited for temperature-sensitive materials with a low viscosity with small quantities of solids. The system has a low-pressure drop and low susceptibility for fouling.
**Applications:**
* Chemical
* Petrochemical
* Polymer
2.5.1 | Falling-film heat exchanger |
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Improvement of multifunctional heat exchangers applied in industrial processes | |
Abstract This article concerns multifunctional heat exchangers. It is comprised of investigations into the improvement of falling film evaporators and rotating disc compact heat exchangers. The mechanism of heat and mass transfer during falling film evaporation of mixtures was studied to establish and improve heat exchange techniques for recycling diluted water-solvent-paint mixtures. Standard model was improved to take into account phenomena such as waves and turbulence in the film. It allowed to predict temperature and concentration profiles along the surface and in the film itself. This analysis was confirmed through experimental measurements with an accurate test facility composed of an electrically heated single vertical tube. Finally, recommendations about the heat and mass transfer surface geometry are suggested and tested with an industrial test rig. The improvement of heat and mass transfer during falling film evaporation of solutions was also studied. It consisted of the use of spiral fin graphite tubes. Modelling of heat transfer from heat carrier to film was done as well as the heat and mass transfer to the vapour, from the film flowing on an external or internal fin. The effect of obstacles was examined. The hydrodynamics of a film flowing along such a surface was studied. An industrial test rig was tested with water and a viscous fluid simulating the evaporation of phosphoric acid solution. With regard to reaction combined with heat and mass transfer, the use of a rotating disc as a reactor was studied. The hydrodynamics of a viscous melt was examined as a function of various parameters such as speed of rotation, flowrate, geometry, physical properties and type of distributor. A device, able to polymerise polystyrene was fabricated and tested. The results show that a spinning disc reactor enhances the reaction rate and reduces significantly the reaction time. Parallel to energy saving, the molecular weight distribution shows a better quality of the delivered polymer. | |
08/01/1997 00:00:00 | |
Link to Article | |
2.5.2 | Falling-film heat exchanger |
Performance improvement of a falling-film-type heat exchanger by insertion of shafts with screw blade in a heat exchanger tube | |
Abstract Highly-efficient heat exchange is expected for the falling-film-type heat exchanger handled in this study by utilizing a falling liquid film, etc. The heat medium is flowed inside the heat exchanger tube. In contrast, the falling film is flowed outside the heat exchanger tube, thereby exchanging heat. In the previous study, considering the basic heat transfer characteristic of the falling-film-type heat exchanger, the design equation was developed in the limited extent. In this study, focusing on the flow condition in a heat exchanger tube of the falling-film-type heat exchanger, various shafts with screw blade were inserted in a single heat exchanger tube and it was evaluated how the pitch and height of screw and the flow rate of cooling water would give an effect on the heat exchange performance. Additionally, the heat transfer coefficient and the overall heat transfer coefficient of the falling-film-type heat exchanger were logically calculated, and then a theoretical value and an experimental value were compared and evaluated. As a result, it was clarified that the heat exchange performance of the falling-film-type heat exchanger was improved by inserting the shaft with screw blade, and theoretical and experimental values were roughly matched. | |
06/01/2016 00:00:00 | |
Link to Article | |
2.6 Helical baffled heat exchanger
The efforts to improve the shell side flow characteristics are made using the spiral baffle plates instead of vertical baffle plates. In this type of heat exchanger, fluid contacts with tubes flowing rotationally in the shell. It could improve heat exchanger performance considerably because stagnation portions in the shell could be removed. It is proved that the shell-and-tube heat exchanger with spiral baffle plates is superior to the conventional heat exchanger in terms of heat transfer. Art. [#ARTNUM](#article-26213-1536994987) The required heat transfer can be reduced up to 35%. Furthermore, it can be used to reduce the created pressure drop, damaging vibrations and acoustic rumbling. The shell-side fouling is also reduced which allows for extended operating time.
2.6.1 | Helical baffled heat exchanger |
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An Experimental Study of Shell-and-Tube Heat Exchangers With Continuous Helical Baffles | |
Two shell-and-tube heat exchangers (STHXs) using continuous helical baffles instead of segmental baffles used in conventional STHXs were proposed, designed, and tested in this study. The two proposed STHXs have the same tube bundle but different shell configurations. The flow pattern in the shell side of the heat exchanger with continuous helical baffles was forced to be rotational and helical due to the geometry of the continuous helical baffles, which results in a significant increase in heat transfer coefficient per unit pressure drop in the heat exchanger. Properly designed continuous helical baffles can reduce fouling in the shell side and prevent the flow-induced vibration as well. The performance of the proposed STHXs was studied experimentally in this work. The heat transfer coefficient and pressure drop in the new STHXs were compared with those in the STHX with segmental baffles. The results indicate that the use of continuous helical baffles results in nearly 10% increase in heat transfer coefficient compared with that of conventional segmental baffles for the same shell-side pressure drop. Based on the experimental data, the nondimensional correlations for heat transfer coefficient and pressure drop were developed for the proposed continuous helical baffle heat exchangers with different shell configurations, which might be useful for industrial applications and further study of continuous helical baffle heat exchangers. This paper also presents a simple and feasible method to fabricate continuous helical baffles used for STHXs. | |
01/01/2007 00:00:00 | |
Link to Article | |
2.6.2 | Helical baffled heat exchanger |
Analysis of Segmental and Helical Baffle in Shell and tube Heat Exchanger | |
In this project work the analyze of two different baffle in a Shell and Tube Heat Exchanger done by ANSYS FLUENT. Shell and tube heat exchanger has been widely used in many industrial applications such as electric power generation, Refrigeration and Environmental Protection and Chemical Engineering. Baffle is an shell side Component of shell and tube heat exchanger The segmental baffle forces the liquid in a Zigzag flow and improving heat transfer and a high pressure drop and increase the fouling resistance and Helical Baffle have a Effective Performance of increasing heat transfer performance. The desirable features of heat exchanger obtain a maximum heat transfer Coefficient and a lower pressure drop. From the Numerical Experimentation result the performance of heat exchanger is increased in Helical Baffle instead of Segmental Baffle | |
01/01/2014 00:00:00 | |
Link to Article | |
2.6.3 | Helical baffled heat exchanger |
Baffle space impact on the performance of helical baffle shell and tube heat exchangers | |
Abstract Heat exchange devices are essential components in complex engineering systems related to energy generation and energy transformation in industrial scenes. Modelling of shell and tube heat exchanger, for design and performance evaluation, is now an established technique in industrial fields. In this paper, heat exchangers with non-continuous helical baffles based on periodic boundaries have been simulated by using commercial code of FLUENT. All possible attempts were made to obtain the influence of baffle spaces on fluid flow and heat transfer on the shell side of by using the same geometrical and thermo-physical conditions. Helical baffles corresponded to the helix angles of 40°, and 5 heat exchangers with different baffle spaces were designed. Designed baffle spaces are: for case A: 15 mm (a minimum elected space), for case B: P/16, for case C: P/8 (middle-overlap type), for case D: 3P/16 and for case E: P/4 (end-to-end type). P refers to helix pitch. The results of simulations indicate that for the same mass flow rate, the heat transfer per unit area decreases with the increase of baffle spaces; however, for the same pressure drop, the most extended baffle space (Case E) obtains higher heat transfer. We also found out that the pressure gradient decreases with the increase of baffles space. | |
11/01/2012 00:00:00 | |
Link to Article | |
2.6.4 | Helical baffled heat exchanger |
Performance of a shell-and-tube heat exchanger with spiral baffle plates | |
School of Mechanical and Industrial System Engineering, Dong-Eui University, Busan 614-714, Korea In a conventional shell-and-tube heat exchanger, fluid contacts with tubes flowing up and down in a shell, therefore there is a defect in the heat transfer with tubes due to the stagnation portions. Fins are attached to the tubes in order to increase heat transfer efficiency, but there exists a limit. Therefore, it is necessary to improve heat exchanger performance by changing the fluid flow in the shell. In this study, a highly efficient shell-and-tube heat exchanger with spiral baffle plates is simulated three-dimensionally using a commercial thermal-fluid analysis code, CFX4.2. In this type of heat exchanger, fluid contacts with tubes flowing rotationally in the shell. It could improve heat exchanger performance considerably because stagnation portions in the shell could be removed. It is proved that the shell-and-tube heat exchanger with spiral baffle plates is superior to the conventional heat exchanger in terms of heat transfer. | |
11/01/2001 00:00:00 | |
Link to Article | |
2.6.5 | Helical baffled heat exchanger |
Research and Industry Application of Helical Baffled Heat Exchangers | |
The helical baffled heat exchanger mainly includes two kinds of different geometry designs.The first is that helical baffles are not integrally continuous and a central tube is not placed in the exchanger.The second is that helical baffles are integrally continuous and a central tube is placed in the exchanger.The research works concerning hydrodynamic studies,and heat transfer and pressure drop testes and numerical simulations in the shell side of helical baffled heat exchangers are reviewed.The application of the helical baffled heat exchangers combined with different enhanced tubes are presented.Eventually,the expected aspects of further investigations on helical baffled heat exchangers are put forward. | |
01/01/2008 00:00:00 | |
Link to Article | |
2.6.6 | Helical baffled heat exchanger |
Research and Industry Application of the Helically Baffled Heat Exchanger | |
The helically baffled heat exchanger mainly includes two kinds of different geometry designs. The first is that helical baffles are not integrally continuous and a central tube is not placed in the exchanger, the second is that helical baffles are integrally continuous and a central tube is placed in the exchanger. The research works concerning hydrodynamic studies, heat transfer and pressure drop testes and numerical simulations in the shell side of helically baffled heat exchanger are reviewed, and the application on the helically baffled heat exchangers combined with different enhanced tubes are presented. Eventually, the expected aspects of further investigations on helically baffled heat exchanger are put forward. | |
01/01/2008 00:00:00 | |
Link to Article | |
2.7 ROD baffled heat exchanger
The ROD baffle heat exchanger can slightly enhance the shell side heat transfer coefficient with the significant reduction of pressure loss due to the shell side fluid flowing longitudinally through a tube bundle, which leads to the reduction of the manufacture and running cost and in some cases to the dimensions reduction of the heat exchangers. Art. [#ARTNUM](#article-26129-2047878495)
The RODbaffle exchanger offers a solution to the vexing problem of tube failures in shell-and-tube exchangers resulting from tube vibration. Thus the RODbaffled heat exchanger is used when the pressure drop or damaging vibration is a crucial constraint.
Supplier
2.7.1 | ROD baffled heat exchanger |
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3D Simulation on the Unit Duct in the Shell Side of the ROD Baffle Heat Exchanger | |
The ROD baffle heat exchanger can slightly enhance the shell side heat transfer coefficient with the significant reduction of pressure loss due to the shell side fluid flowing longitudinally through tube bundle, which leads to the reduction of the manufacture and running cost and in some cases to the dimensions reduction of the heat exchangers. Because of the complexities of fluid dynamics equations and the structure of heat exchangers, few theoretical researches have been accomplished to specify the shell side characteristics of the ROD baffle heat exchanger. A unit duct model in the shell side of the longitudinal flow type heat exchanger has been developed based on suitable simplification. A numerical analysis on shell side of the ROD baffle heat exchanger has been carried out at constant wall temperature to obtain the characteristics of heat transfer and pressure drop. The numerical results show that the ROD baffles placed vertically and horizontally in the unit duct continue to shear and comminute the streamline flow when the fluid crosses over the ROD-baffles, and change the fluid flow directions, and then the continuity and stability of the fluid are destroyed. The effect of disturbing flow can promote fluid turbulent intensity and effectively enhance heat transfer. The numerical analyses can provide the theoretical bases for optimizing the structure of ROD baffle heat exchanger and improving its performance. | |
08/01/2006 00:00:00 | |
Link to Article | |
3. Other tubular
BackNext to shell and tube heat exchangers, other tubular heat exchangers are presented.
3.1 Double pipe heat exchanger (DPHE)
One of the most simple and applicable heat exchangers is double pipe heat exchanger (DPHE), also called the concentric tube heat exchanger. This kind of heat exchanger is widely used in chemical, food, oil and gas industries. Upon having a relatively small diameter, many precise studies have also held firmly the belief that this type of heat exchanger is used in high-pressure applications. They are also of great importance where a wide range of temperature is needed. Art. [#ARTNUM](#article-26215-2519485646)
The system is a simple compact design which is resistant against thermal fatigue. For a single unit capacities of 29 kW with a liquid flow of 2.3 m³/hr are shown. The simple systems allow for easy maintenance.
The performance of the heat exchanger and the pressure drop are in close interaction with the geometry. Art. [#ARTNUM](#article-26215-2771080156)
**Applications:**
* High temperature, high pressure, low flow
* Multi-phase fluids & slurries
* High thermal stress
* Steam condensing
* Seal cooling
* Liquid/Gas
* Sampling
* Sewage sludge heating
* Effluent water cooling
* Food
* Detergents and dyes
3.1.1 | Double pipe heat exchanger (DPHE) |
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A comprehensive review on double pipe heat exchangers | |
Abstract Growing need to develop and improve the effectiveness of heat exchangers has led to a broad range of investigations for increasing heat transfer rate along with decreasing the size and cost of the industrial apparatus accordingly. One of these many apparatus which are used in different industries is double pipe heat exchanger. This type of heat exchanger has drawn many attentions due to simplicity and wide range of usages. In recent years, several precise and invaluable studies have been performed in double pipe heat exchangers. In this review, the development procedure that this type of heat exchanger went through has been analyzed in details and the heat transfer enhancement methods in aforementioned heat exchangers have also been widely discussed. Having also tried the best to present a comprehensive research, the authors gathered information regarding the usage of these methods such as active, passive and compound methods which is worth noting that the studies concerning using passive methods in double pipe heat exchangers have been frequently cited. Moreover, various studies concerning using nanofluids in double pipe heat exchangers have been discussed in details. In this review, correlations of mostly Nusselt number and pressure drop coefficient are also presented. It is believed that this review provides new insights for further investigations. | |
01/01/2017 00:00:00 | |
Link to Article | |
3.1.2 | Double pipe heat exchanger (DPHE) |
Analytical and Numerical Design Analysis of Concentric Tube Heat Exchangers – A Review | |
This paper considers an analytical and a numerical approach in the design of a concentric tube heat exchanger. Sensible heat transfer is considered in the analysis and the heat exchanger is developed for actual operating conditions in a chemical plant. The heat exchanger is a concentric tube heat exchanger where hot oil exchanges heat with hot water. Hot oil is in the inner pipe and the heating medium, hot water, is in the outer pipe (annular side) of the heat exchanger. An analytical model employing effectiveness-number of transfer units (e-NTU) approach and log mean temperature difference (LMTD) approach were employed in the design of the concentric tube heat exchanger. In the design process, performance charts were developed for concentric tube heat exchanger. Performance charts describe the performance of the heat exchanger in terms of crucial dimensionless parameters. Performance charts help to select the right number of transfer units (NTU) for the given heat exchanger. Both parallel and counter flow configurations were considered for the design analysis. Likewise, a numerical model was also considered in the design of the heat exchanger. The results from the analysis are presented and compared. From the results it can be seen that both numerical and analytical approaches produce the exact same results. The designer certainly has the flexibility to choose an appropriate design methodology based on the available inputs and requirements. | |
12/01/2017 00:00:00 | |
Link to Article | |
3.1.3 | Double pipe heat exchanger (DPHE) |
Analytical Investigation on Effect of Nanofluid Usage on Temperature Distribution in Double Pipe Heat Exchangers | |
Heat exchangers are used in many industrial areas for the purpose of meeting the heat transfer requirement. The widespread use of heat exchangers has led to a number of designs for increasing the heat transfer in the heat exchangers. One of the widely used heat exchanger types is the double pipe heat exchangers. In this study, the effects of nanofluid usage on temperature distribution in double pipe heat exchangers have been investigated analytically for laminar and steady-state flow conditions at a certain Reynolds number. Alumina based nanofluid with different particle sizes and water were used as heat transfer fluid in the inner and outer pipes and the fluid temperatures were compared with each other for all conditions. In addition that, for this conditions, the analytical results confirmed with the numerical results. | |
07/30/2017 00:00:00 | |
Link to Article | |
3.1.4 | Double pipe heat exchanger (DPHE) |
Optimal Design of Double-Pipe Heat Exchangers | |
Heat exchangers are used in industrial and household processes to recover heat between two process fluids. This paper shows numerical investigations on heat transfer in a double pipe heat exchanger. The working fluids are water, and the inner and outer tube was made from carbon steel. There are several constructions which able to transfer the requested heat, but there is only one geometry which has the lowest cost. This cost comes from the material cost, the fabrication cost and the operation cost. These costs depend on the material types and different geometric sizes, for example inner pipe diameter, outer pipe diameter, length of the tube. The performance of the heat exchanger and the pressure drop are in a close interaction with the geometry. Optimum sizes can be calculated from the initial conditions (when one of the process fluid inlet and outlet temperature and the flow rate is specified). The correlations to the Nusselt number and the friction data come from experimental studies. | |
06/05/2017 00:00:00 | |
Link to Article | |
3.1.5 | Double pipe heat exchanger (DPHE) |
Optimum design of double pipe heat exchanger | |
Heat exchangers are used in industrial processes to recover heat between two process fluids. Although the necessary equations for heat transfer and the pressure drop in a double pipe heat exchanger are available, using these equations the optimization of the system cost is laborious. In this paper the optimal design of the exchanger has been formulated as a geometric programming with a single degree of difficulty. The solution of the problem yields the optimum values of inner pipe diameter, outer pipe diameter and utility flow rate to be used for a double pipe heat exchanger of a given length, when a specified flow rate of process stream is to be treated for a given inlet to outlet temperature. | |
05/01/2008 00:00:00 | |
Link to Article | |
3.2 Triple concentric tube heat exchanger (TCTHE)
In the TCTHE, there are three sections: central tube, inner annular space and outer annular space. Heat transfer mediums are passed through the central tube and outer annular space and a thermal fluid is passed through inner annular space. This type of heat exchanger can be used for higher viscosity fluids.
The triple tube heat exchanger contributes to higher heat exchanger effectiveness and more energy saving compared with double tube heat exchanger per unit length. Art. [#ARTNUM](#article-26134-2245358019)
**Applications:**
* Food
3.2.1 | Triple concentric tube heat exchanger (TCTHE) |
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Analysis of the heat transfer in double and triple concentric tube heat exchangers | |
The tubular heat exchangers (shell and tube heat exchangers and concentric tube heat exchangers) represent an important category of equipment in the petroleum refineries and are used for heating, pre-heating, cooling, condensation and evaporation purposes. The paper presents results of analysis of the heat transfer to cool a petroleum product in two types of concentric tube heat exchangers: double and triple concentric tube heat exchangers. The cooling agent is water. The triple concentric tube heat exchanger is a modified constructive version of double concentric tube heat exchanger by adding an intermediate tube. This intermediate tube improves the heat transfer by increasing the heat area per unit length. The analysis of the heat transfer is made using experimental data obtained during the tests in a double and triple concentric tube heat exchanger. The flow rates of fluids, inlet and outlet temperatures of water and petroleum product are used in determining the performance of both heat exchangers. Principally, for both apparatus are calculated the overall heat transfer coefficients and the heat exchange surfaces. The presented results shows that triple concentric tube heat exchangers provide better heat transfer efficiencies compared to the double concentric tube heat exchangers. | |
08/01/2016 00:00:00 | |
Link to Article | |
3.2.2 | Triple concentric tube heat exchanger (TCTHE) |
Experimental and numerical investigations of a triple concentric-tube heat exchanger | |
Abstract The experimental and numerical investigations of the triple concentric-tube heat exchanger are presented with particular reference to double tube heat exchanger. The purpose is to present a clear view on the thermo-fluid characteristics of this type of heat exchangers with different key design parameters leading to design optimization. Three fluids being considered are chilled water in inner tube, hot water in inner annulus, and normal tap water in outer annulus. Numerical CFD model is developed using a finite volume discretization method. The numerical model is validated and then extended to cover more extra design parameters. Four flow patterns are conducted of counter current, co-current, counter current with co-current and co-current with counter current flow. Correlations of Nusselt number, friction factor and heat exchanger effectiveness with the dimensionless design parameters are also presented. The triple tube heat exchanger contributes higher heat exchanger effectiveness and more energy saving compared with double tube heat exchanger per unit length. | |
04/01/2016 00:00:00 | |
Link to Article | |
3.2.3 | Triple concentric tube heat exchanger (TCTHE) |
Numerical Analysis of Triple Concentric Tube Heat Exchanger using Dimpled Tube Geometry | |
Computational Fluid Dynamic (CFD) is a useful tool in solving and analyzing problems that involve fluid flows, while triple tube concentric tube heat exchanger is the most common type of heat exchanger and widely use in chemical and food processes. In this current research to studying the Numerical Analysis of Triple Concentric Tube Heat Exchanger Using spherical shape of the Dimpled Tube Geometry, it's to create modeling and meshing the Plain and spherical dimpled geometry of triple tube concentric tube heat exchanger using the CFD package Gambit 2.4 and the boundary condition to be set before been simulate in Fluent 6.2 based on the parameters. The Hot water is flowing through in an Intermediate tube and Cold water is flowing through in an inner tube and outer tube at different Reynolds numbers. Triple Concentric tube heat exchanger performance is compared with plain and spherical shape dimpled triple concentric tube heat exchanger using CFD. From this result the simulation of in triple concentric tube heat exchanger enhancing spherical dimpled tube model to increasing the overall heat transfer coefficient, effectiveness and heat transfer rate compare to plain tube, and also calculate the flow characteristics of velocity, Nusselt number, pressure drop and Friction factor of the triple concentric tube heat exchanger spherical dimpled tube. | |
01/01/2016 00:00:00 | |
Link to Article | |
3.3 Helical coil heat exchanger
Helical coil heat exchangers contain a helical tube. They are a simpler version of a spiral wound heat exchanger.
Helical coils are very alluring for various processes such as heat exchangers and reactors because they can accommodate a large heat transfer area in a small space, with high heat transfer coefficients and narrow residence time distributions.
The modification of the flow in the helically coiled tubes is due to the centrifugal forces. The curvature of the tube produces a secondary flow field with a circulatory motion, which pushes the fluid particles toward the core region of the tube. Thus the application of curved tubes in heat exchange process can be highly beneficial in comparison with the straight tube. These applications can arise in the food processing industry for heating and cooling of highly viscous liquid food, such as pastes, or for products that are sensitive to high shear stresses.
**Advantages:**
* Heat transfer rate in the helical coil is higher as compared to a straight tube heat exchanger. Compact
structure.
* It requires a small amount of floor area compared to other heat exchangers.
* Larger heat transfer surface area.
**Applications:** Art. [#ARTNUM](#article-26208-2593188271)
* Power plants
* Nuclear plants
* Chemical processing
* Refrigeration
* Food
* LNG plants
* Pools/water industry
* Electronics
Suppliers
3.3.1 | Helical coil heat exchanger |
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A REVIEW ON INVESTIGATION OF HELICAL COIL HEAT EXCHANGER | |
Heat exchanger are important engineering system with wide variety of application including power plants, refrigeration and air conditioning system, heat recovery system, nuclear reactors, chemical processing and food industries. Working towards the goal of saving energies and to make concise design for mechanical and chemical devices and plants, heat transfer play major role in design of heat exchangers. We are not use application of external power, but we can improve the heat transfer rate by modifying the design by providing the helical tubes, extended surface or swirl flow devices. We improve the heat transfer rate from helical coil tube-in-tube heat exchangers to use Computational Fluid Dynamics (CFD). My project aims to perform a numerical study of helical coil tube-in-tube heat exchanger with water as both hot and cold fluid. To improve the effectiveness, heat transfer rate and reduce power consumption, D/d geometrical parameter will be varied for different boundary conditions. The impact of this modification on Nusselt number, friction factor, pumping power required and LMTD variation of inner fluid with respect to Reynolds number was studied. | |
01/01/2017 00:00:00 | |
Link to Article | |
3.3.2 | Helical coil heat exchanger |
A Review on Investigation of Performance of Pipe in Pipe Helically Coil Heat Exchanger | |
Enhancing the heat transfer by the use of helical coils has been studied and researched by many researchers, because the fluid dynamics inside the pipes of a helical coil heat exchanger offer certain advantages over the straight tubes, shell and tube type heat exchanger, in terms of better heat transfer and mass transfer coefficients. This configuration offers a high compact structure and a high overall heat transfer coefficient; hence helical coil heat exchangers are widely used in industrial applications. Convective heat transfer between a surface and the surrounding fluid in a heat exchanger has been a major issue and a topic of study in the recent years. In this particular study, an attempt has been made to experimental work of various parameters like radius of tubes, pitch of coil, pitch circle diameter, number of turns of helical coil, flow rate and temperature that affect the effectiveness of a heat exchanger and increases heat transfer rate at two different flows (parallel and counter-flow)on the total heat transfer from a helical tube, where the cold fluid flows in the outer pipe and the hot fluid flowing in the inner pipes of the pipe in pipe helical coiled heat exchanger. This paper focus on the review on helically coiled heat exchanger. | |
07/01/2015 00:00:00 | |
Link to Article | |
3.3.3 | Helical coil heat exchanger |
An Empirical Study of Helical Coil Heat Exchanger Used in Liquid Evaporization and Droplet Disengagement for a Laminar Fluid Flow | |
Heat exchanger is an important component in industrial systems especially in process industries. Many commercial designs and types of heat exchangers are available in market for transfer of heat as well as for recovery of waste heat for the process plants. As helical coil have compact size and higher heat transfer coefficient they are widely used in industrial applications such as food preservation, refrigeration, process plant, power generation, etc. An attempt has been made to study the parallel flow and counter flow of inner higher temperature fluid flow and lower temperature fluid flow, which are separated by copper surface in a helical coil heat exchanger. Helical geometry allows the effective handling at higher temperatures and extreme temperature differentials without any highly induced stress or expansion of joints. These heat exchanger consists of series of stacked helical coiled tubes and the tube ends are connected by manifolds, which also acts as fluid entry and exit locations. In this paper, we focus on design parameters and heat transfer conditions of a vaporizer or generator of a simple vapour absorption refrigeration system having flow condition of refrigerant taken as laminar flow. | |
01/01/2014 00:00:00 | |
Link to Article | |
3.3.4 | Helical coil heat exchanger |
Experimental Investigation of Performance of Pipe in Pipe Helically Coil Heat Exchanger and Validation using CFD FLUENT | |
Enhancing the heat transfer by the use of helical coils has been studied and researched by many researchers, because the fluid dynamics inside the pipes of a helical coil heat exchanger offer certain advantages over the straight tubes, shell and tube type heat exchanger, in terms of better heat transfer and mass transfer coefficients. This configuration offers a high compact structure and a high overall heat transfer coefficient; hence helical coil heat exchangers are widely used in industrial applications. Convective heat transfer between a surface and the surrounding fluid in a heat exchanger has been a major issue and a topic of study in the recent years. In this particular study, an attempt has been made to experimental work of various parameters like radius of tubes, pitch of coil, pitch circle diameter, number of turns of helical coil, flow rate and temperature that affect the effectiveness of a heat exchanger and increases heat transfer rate at two different flows (parallel and counter-flow) on the total heat transfer from a helical tube, where the cold fluid flows in the outer pipe and the hot fluid flowing in the inner pipes of the pipe in pipe helical coiled heat exchanger. The results obtaining from the experiment conducted on test rig of pipe in pipe helical coil heat exchanger are to be validated by Computational fluid dynamics (CFD) in ANSYS FLUENT 14.0. Copper was chosen as the as metal for the construction of the helical tube. The fluid flowing through the tube was taken as water. Key words — Helical coil heat exchangers, Parallel flow and Counter flow, coil configuration, CFD. | |
06/14/2015 00:00:00 | |
Link to Article | |
3.4 Spiral wound heat exchanger (SWHE)
A spiral wound heat exchanger is very compact heat exchanger composed of spiralled coils. It can be used in a shell and tube type of exchanger. They can also be used for multi-phase and multi-stream applications. They are commonly used in large-scale applications: Refinery plants; (petro)chemical plants.
**Research findings:**
* Spiral wound heat exchanger (SWHE) has been used as the main cryogenic heat exchanger in 90% of land-based liquefied natural gas (LNG) plants, due to the advantages of compact structure, high-pressure resistance, large scale unit, good thermal compensation performance and multi-stream heat transfer capability. Art. [#ARTNUM](#article-26124-2748655173)
* A spiral-wound heat exchanger (SWHE) has many significant advantages over other heat exchangers, such as high robustness, high effectiveness and large exchanger area per volume. As such, it has been widely used in liquefied natural gas (LNG) plants, air separation plants, petroleum plants and nuclear reactor plants. Especially in the large-scale land-based LNG plants and offshore floating LNG plants, the SWHE is the preferred choice of the main cryogenic heat exchanger. Art. [#ARTNUM](#article-26124-2774313722)
Applications:
* Liquid-to-liquid
* Cryogenic
* High pressure
* Natural gas heaters
* Vent condensers
* Mechanical seal coolers
* Compressor inter/aftercoolers
* Supercritical fluid
* Water heaters
* Steam or process fluid vaporizers
* Boiler or process sample coolers
* LNG plants
* Petroleum/ air separation and nuclear reactor plants.
3.4.1 | Spiral wound heat exchanger (SWHE) |
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DESIGN AND FABRICATION OF SPIRAL COILED RADIATOR | |
Spiral tube heat exchangers are known as excellent heat exchanger because of far compact and high heat transferefficiency. An innovative spiral tube heat exchanger is designed for particular process engineering. A new arrangement for flow of hot and cold fluids is employed for design, hot fluid flows in axial path while the cold fluid flows in a spiral path. To measure the performance of the spiral tube heat exchanger, its model is suitably designed and fabricated so as to perform experimental tests. The paper gives analysis of spiral tube heat exchanger over the shell and tube heat exchanger. | |
01/01/2018 00:00:00 | |
Link to Article | |
3.4.2 | Spiral wound heat exchanger (SWHE) |
Experimental investigation on downward flow boiling heat transfer characteristics of propane in shell side of LNG spiral wound heat exchanger | |
Abstract For designing LNG spiral wound heat exchangers (SWHE), the boiling heat transfer mechanism of two-phase hydrocarbon refrigerant flowing downward in shell side should be known. In this study, an explosion-proof experimental rig was established for measuring heat transfer coefficients (HTC) and observing flow patterns. The test section contains three-layer tube bundles to emulate the actual structure and flow conditions of an SWHE. Propane as one main component of shell-side refrigerant is used as the tested fluid. The experimental conditions cover heat fluxes of 4~10 kW⋅m −2 , mass fluxes of 40~80 kg (m 2 ⋅s) −1 and vapor qualities of 0.2~1.0. The results indicate that HTC initially increases and then decreases with the increment of vapor quality, representing a maximum at a vapor quality of 0.8~0.9; the effect of heat flux on HTC increases with the increment of heat flux. A correlation of HTC was developed covering 98% of the experimental data within a deviation of ±20%. | |
12/01/2017 00:00:00 | |
Link to Article | |
3.4.3 | Spiral wound heat exchanger (SWHE) |
Geometrical Parametric Analysis of Flow and Heat Transfer in the Shell Side of a Spiral-Wound Heat Exchanger | |
The spiral-wound heat exchangers are widely used in chemical industrial applications, but the mechanism of flow and heat transfer in shell side has not been clarified yet. A three-dimensional model is developed based on the FLUENT software in this study, with emphasis on quantifying the effects of the main geometry parameters, such as the number of tube bundles, the number of tube layers, the thickness of space bars, the number of tubes per circle in the first layer, the tube external diameter, the central cylinder diameter, and the tube pitch in the first layer, on the flow and heat transfer. Based on the numerical simulation results, the Taguchi method is used to estimate the effect of these geometrical factors on flow and heat transfer and the contribution rate of every factor is obtained. Meanwhile, the multivariate correlation is developed by MATLAB software to calculate the Nusselt number and friction factor in the shell side. | |
06/13/2015 00:00:00 | |
Link to Article | |
3.4.4 | Spiral wound heat exchanger (SWHE) |
Heat transfer and pressure drop characteristics of two-phase propane flow in shell side of LNG spiral wound heat exchanger | |
Abstract For designing LNG spiral wound heat exchangers (SWHE), the boiling heat transfer and pressure drop characteristics of two-phase hydrocarbon refrigerant flowing downward at shell side should be known. In this study, an explosion-proof experimental rig was established for observing flow patterns and measuring heat transfer coefficients and pressure drops. The test section contained three-layer tube bundles to emulate the actual structure and flow conditions of a SWHE. Propane as one main component of shell-side refrigerant was used as the tested fluid. Through the experimental analysis, the influence laws of vapor quality, mass flux on flow pattern, heat transfer and pressure drop of propane are obtained. As the vapour quality increases, the heat transfer coefficient in the shell side of LNG SWHE initially increases and then decreases, representing a maximum at a vapour quality of 0.8~0.9. The flow patterns in the shell side of LNG SWHE present to be the column falling film flow, droplet falling film flow, shear flow, mist flow and gas flow as the vapour quality increases from 0.2 to 1.0. | |
12/01/2017 00:00:00 | |
Link to Article | |
3.4.5 | Spiral wound heat exchanger (SWHE) |
Numerical investigation on gas flow heat transfer and pressure drop in the shell side of spiral-wound heat exchangers | |
As a critical facility, spiral-wound heat exchanger (SWHE) has been widely used in many industrial applications. A computational fluid dynamics (CFD) model was employed with the smallest periodic element and periodic boundary conditions to examine the characteristics of the shell side of SWHE. Numerical simulation results show that the heat transfer coefficients around the tube initially increase and subsequently decrease with radial angle because of the influence of backflow and turbulent separation. The mean absolute deviation between simulated heat transfer coefficients and measured values for methane, ethane, nitrogen and a mixture (methane/ethane) is within 5% when Reynolds number is over 30000. For the pressure drop, the simulated values are smaller than the measured values, and the mean absolute deviation is within 9%. Numerical simulation results also indicate that the pressure drop and heat transfer coefficients on the shell side of SWHE decrease as the winding angle of the tubes increases. Considering the effect of winding angle on pressure drops and heat transfer coefficients, the modified correlations of Nusselt number Nu = 0.308Re0.64Pr0.36(1 + sinθ)-1.38 and friction factor f = 0.435Re-0.133(sinθ)-0.36, are proposed. Comparing with the experimental data, the maximum deviations for heat transfer coefficients and pressure drops are less than 5% and 11% respectively. | |
04/01/2018 00:00:00 | |
Link to Article | |
4. Extended or Enhanced
BackExtended or enhanced heat exchangers make use of design elements that enhance heat transfer, usually by etending the surface area.
4.1 Plate-fin heat exchanger
A plate-fin heat exchanger is a form of compact heat exchanger consisting of a block of alternating layers of corrugated fins and flat separators known as parting sheets. These heat exchangers can be made in a variety of materials such as aluminium, stainless steels, nickel, copper, etc. depending upon the operating temperatures and pressures. They are widely used in aerospace, automobile and cryogenic industries due to its compactness (i.e., high heat transfer surface-area-to-volume ratio) for desired thermal performance, resulting in reduced space, weight, support structure, footprint, energy requirement and cost.
Depending on the application, various types of augmented heat transfer surfaces such as plain fins, wavy fins, offset strip fins, louvred fins and perforated fins are used. They have a high degree of surface compactness and substantial heat transfer enhancement obtained as a result of the periodic starting and development of laminar boundary layers over interrupted channels formed by the fins and their dissipation in the fin wakes. Art. [#ARTNUM](#article-26207-2013946548)
There are different designs possible, as can be seen in the figure. High thermal efficiencies can be reached up to 90% in heat recovery applications.
**Applications:**
* Cryogenic
* Air separation plants
* Natural gas liquefaction plants
* Petrochemical plants
* Gas treatment plants
* Helium liquefaction plants
Links
4.1.1 | Plate-fin heat exchanger |
---|---|
Comparison of waste heat recovery performances of plate-fin heat exchangers produced from different materials | |
High amount of waste heat emerging from thermal processes performed in the industry can be recovered by means of equipment such as heat pipes, heat exchangers and heat recovery boilers. In this study, thermal performance of a heat recovery device, which enables air-to-air heat transfer, was examined. For this purpose, cross-flow plate-fin heat exchangers were produced by using three different materials, which are aluminum, polymer and cellulose. With the established apparatus, outlet temperatures with different values were obtained for fresh air and exhaust air. Thermal calculations, were performed with the mathematical model developed by using the EffectivenessNumber of Transfer Unit (e NTU) method and their results were compared. It was seen that at the same air rate with the same exhaust air inlet temperature and the same fresh air inlet temperature; when the polymer heat exchanger is used, effectiveness value is 12,6% higher on an average than the aluminum heat exchanger. Similarly, when the cellulose heat exchanger is used, effectiveness value is 14,5% higher on an average than the polymer heat exchanger. | |
01/01/2015 00:00:00 | |
Link to Article | |
4.1.2 | Plate-fin heat exchanger |
Development and validation of a direct passage arrangement method for multistream plate fin heat exchangers | |
Abstract Passage arrangement quality significantly affects the performance of multistream plate fin heat exchanger (MPFHEs) because a bad arrangement may result in uneven temperature difference field and pressure field between passages and thus reduce the thermal efficiency. However, it is very difficult to design an effective passage arrangement owing to large numbers of possible passage arrangement patterns and complex heat transfer processes between the passages in a MPFHE. This work develops a direct passage arrangement method for MPFHEs to address this problem. In this method, an improvement of passage arrangement with good synergistic heat transfer effect is first proposed. The determination of passage quantity for each fluid is suggested to be proportional to its design heat load. Next, based on the results of the checking calculation, the fin and heat exchanger structure parameters should be adjusted until the constraints including thermal effectiveness, length deviation and pressure drops have been satisfied. Afterwards, the passages are arranged directly by a symmetry arrangement method. To evaluate the effectiveness of this method, three different industrial cases are performed and compared with the existing optimization designs by three evaluation means. The validation results indicate that this method performs better than the complex optimization methods. | |
02/01/2018 00:00:00 | |
Link to Article | |
4.1.3 | Plate-fin heat exchanger |
Experimental Analysis of Performance of Heat Exchanger with Plate Fins and Parallel Flow of Working Fluids | |
Heat exchangers are devices in which heat is transferred from one fluid to another fluid as a result of temperature difference. Heat exchanger presented in the current paper in which inside the tubes flows water, but outside the tubes flows air aims to enable cooling of circulating water, which serves to cool the engine of a machine. Such exchangers find application in the automotive industry as well as heating and cooling equipment and HVAC systems etc. The surface of the heat exchanger by the air side always tends to be much larger using surface fins in order to facilitate equalization of thermal resistance for both sides of the heat exchanger, because the rate of transmission of heat from the water side is much greater. Furthermore, the paper will present analytical and experimental studies involved for determination of performance of plate-fin heat exchanger for various flows of working fluids in order to get the highest values of performances i.e.: overall heat transfer coefficient U, efficiency of heat exchanger e, maximal and real heat transferred, pressure drop, air velocity and Reynolds number from the air side of heat exchanger etc. The present scientific paper is based on the fact that from the experimental model made for laboratory conditions, conclusions are derived that can be used during installation of such heat exchanger on certain machines in order to predict their performance. | |
01/01/2017 00:00:00 | |
Link to Article | |
4.1.4 | Plate-fin heat exchanger |
Experimental Investigation on Fluid Flow Maldistribution in Plate-Fin Heat Exchangers | |
The plate-fin heat exchanger is normally designed with the assumption that the fluid is uniformly divided among all the parallel passages. In practice, however, the design of the exchanger, the heat transfer process, the operation of the external system, etc., may create high flow maldistribution. The performance deterioration of plate-fin heat exchangers due to flow maldistribution may be serious. In this review, the flow distribution performance in a plate-fin heat exchanger has been experimentally studied and the distribution performance of different distributors' inlet angles has been measured. The combined effects of the inlet angle and mass flow rate on flow maldistribution have been studied. The study is useful in the optimum design of plate-fin heat exchangers. | |
07/01/2003 00:00:00 | |
Link to Article | |
4.1.5 | Plate-fin heat exchanger |
Studies on pumping power in terms of pressure drop and heat transfer characteristics of compact plate-fin heat exchangers--A review | |
Renewable energy sources like solar energy, wind energy, etc. are profusely available without any limitation. Heat exchanger is a device to transfer the energy from one fluid to other fluid for many applications in buildings, industries and automotives. The optimum design of heat exchanger for minimum pumping power (i.e., minimum pressure drop) and efficient heat transfer is a great challenge in terms of energy savings point of view. This review focuses on the research and developments of compact offset and wavy plate-fin heat exchangers. The review is summarized under three major sections. They are offset fin characteristics, wavy fin characteristics and non-uniformity of the inlet fluid flow. The various research aspects relating to internal single phase flow studied in offset and wavy fins by the researchers are compared and summarized. Further, the works done on the non-uniformity of this fluid flow at the inlet of the compact heat exchangers are addressed and the methods available to minimize these effects are compared. | |
01/01/2010 00:00:00 | |
Link to Article | |
4.2 Finned tube heat exchanger
Finned tube heat exchangers have tubes with extended outer surface area or fins to enhance the heat transfer rate from the additional area of fins. Finned tubes or tubes with extended outer surface area enhance the heat transfer rate by increasing the effective heat transfer area between the tubes and surrounding fluid. There are several types of fins. [\[Source\]](https://www.enggcyclopedia.com/2012/03/finned-tube-heat-exchangers/)
Fin and tube heat exchangers are most widely used due to the extended surface for heat transfer in many industrial applications such as waste heat recovery units, heating, ventilation, and air conditioning and refrigeration systems. Art. [#ARTNUM](#article-26132-2470079271)
Several designs exist for the fins, as can be seen from the figures. New heat exchange tube types with higher performance have been designed, such as the 3-D finned tube, spiral finned tube, serrated finned tube, H-type finned tube, slotted finned tube and so on. Art. [#ARTNUM](#article-26132-2900762659)
Finned tubes are often employed in cooling applications. With the finned tubes, heat recovery up to 90% can be reached. And the maintenance of the finned tube is considered as low.
**Applications:**
* HVAC
* Energy
* Oil and gas
* Petrochemical
* Air cooling
* Chemical
4.2.1 | Finned tube heat exchanger |
---|---|
A comprehensive review on double pipe heat exchangers | |
Abstract Growing need to develop and improve the effectiveness of heat exchangers has led to a broad range of investigations for increasing heat transfer rate along with decreasing the size and cost of the industrial apparatus accordingly. One of these many apparatus which are used in different industries is double pipe heat exchanger. This type of heat exchanger has drawn many attentions due to simplicity and wide range of usages. In recent years, several precise and invaluable studies have been performed in double pipe heat exchangers. In this review, the development procedure that this type of heat exchanger went through has been analyzed in details and the heat transfer enhancement methods in aforementioned heat exchangers have also been widely discussed. Having also tried the best to present a comprehensive research, the authors gathered information regarding the usage of these methods such as active, passive and compound methods which is worth noting that the studies concerning using passive methods in double pipe heat exchangers have been frequently cited. Moreover, various studies concerning using nanofluids in double pipe heat exchangers have been discussed in details. In this review, correlations of mostly Nusselt number and pressure drop coefficient are also presented. It is believed that this review provides new insights for further investigations. | |
01/01/2017 00:00:00 | |
Link to Article | |
4.2.2 | Finned tube heat exchanger |
Design and optimization of a novel high temperature heat exchanger for waste heat cascade recovery from exhaust flue gases | |
Abstract The waste heat of high temperature exhaust flue gases is widely distributed in many industrial processes. Recovery of waste heat is of great significance to energy saving and sustainability. In this paper, a novel high temperature heat exchanger with hybrid enhancement technologies is proposed to improve waste heat recovery efficiency based on the cascade recovery and utilization method. Algorithm for HTHE structural design and optimization is developed and verified according to the experimental results. Heat transfer and pressure drop performance of the proposed HTHE are estimated by using the algorithm. The results show that the effectiveness of the proposed HTHE increases as the gas temperature increases and mass flow rate decreases. Average effectiveness of the proposed HTHE and temperature of preheated air are 12.5% and 85.8 °C higher than those of traditional HTHE with additional 70.0% and 22.0% pressure drop on air and gas sides, respectively. The structural optimization of the proposed HTHE is carried out and it shows that the optimized HTHE has better heat transfer capacity and comprehensive performance under identical pressure drop, increasing effectiveness by 12.6% without enlarging pressure drop compared with the non-optimized HTHE. | |
10/01/2018 00:00:00 | |
Link to Article | |
4.2.3 | Finned tube heat exchanger |
Determination of local heat transfer coefficient distribution on a vortex enhanced finned-tube heat exchanger fin using infrared thermography | |
An innovative vortex-enhanced finned-tube heat exchanger geometry combining winglet longitudinal vortex generators and deflectors guiding the flow in tube wake has been experimentally studied by means of an infrared-based experimental method that allows the local heat transfer coefficient evaluation over the fin. The coefficient distribution is determined by using a transient technique and by calculating the energy balance during the fin cooling. The calculation model takes into account radiation with the surrounding and lateral heat conduction into the material. Results of local heat transfer coefficient distribution are presented for different Reynolds number values. The experimental convective heat transfer fields are first compared with CFD numerical results. A comparative analysis of heat transfer rates vs the smooth fin geometry is then presented. The present experiments were conducted in an open-circuit wind tunnel, see Fig. 1. The upstream part of the wind tunnel has a section with airflow conditioning elements (fibreglass screen, honeycomb flow straightener and converging section) to supply an incoming airflow with uniform cross-sectional distribution and low turbulent level at the inlet of the test section located immediately downstream. Moreover the air temperature in the enclosed upstream chamber is controlled, using an air-conditioning unit, to provide a constant inlet air temperature at the entry of the test section. A rectangular observation window has been air-tightly set into the top-wall of the test section right above the plate fin and tube assembly to allow the measurement of the fin surface temperature. The axial airflow in the wind tunnel is driven by a fan located downstream and its volumetric flow rate is determined using a micro-manometer measuring the pressure drop across an orifice plate flowmeter. A long wave IR camera (AGEMA® Thermovision 900) with a 10° lens is placed at its minimal focalisation distance right above the heat exchanger model which surface has been thinly coated with black coating having high emissivity (95%). The aforementioned rectangular observation window being transparent to infrared radiations, quantitative thermography measurement of the fin surface temperature is then made possible. This window, made of Zinc Selenide, has a direct transmission factor equal to 98 % for infrared wavelengths ranging from 8 to 12 m. The non-interlaced frames recorded by the infrared camera at a frequency equal to 15 Hz are post processed by a specific high accuracy signal-conditioning unit (ADDELIE ®). Finally, for a high accuracy, an in-situ calibration of the | |
01/01/2014 00:00:00 | |
Link to Article | |
4.2.4 | Finned tube heat exchanger |
EXPERIMENTAL INVESTIGATION OF DOUBLE-PIPE HEAT EXCHANGER WITH HELICAL FINS ON THE INNER ROTATING TUBE | |
Heat exchanger is an important device in all the thermal systems. The heat exchanger is widely used equipment in different industries such as process, petroleum refining, chemicals and paper etc. Energy and material saving considerations as well as environmental challenges in the industry have stimulated the demand for high efficiency heat exchanger. To improve the efficiency of heat exchanger one must think of heat transfer enhancement in heat exchanger. Moreover heat transfer enhancement enables the size of heat exchanger to be considerably decreased. A high rate of heat transfer with minimum space requirement is necessity for compact heat exchanger. In present work, to improve the heat transfer characteristic of the double pipe heat exchanger, the helical fins were installed on the outer surface of the inner tube and the level of turbulence increased by the rotating the inner tube. The length of heat exchanger was 1m and the pitch of helical fins kept constant equal to 17 mm. The convective heat transfer coefficients were obtained for the stationary as well as rotating inner tube for the counter flow mode using water as cold fluid in the tube side and glycerol as hot fluid in the shell side. The flow rate of cold fluid was kept constant and that of hot fluid was varied. The Nusselt number was calculated for the each speed of the rotation and compared with standard values obtained from Dittus-Boelter equation. The helical fins increases heat transfer area and rotation of the inner tube increases the mixing of fluid particles which is necessary for the convection mode of heat transfer. The Nusselt number increased up to 64 % at 100 rpm compared to stationary inner tube with helical fins. | |
07/25/2014 00:00:00 | |
Link to Article | |
4.2.5 | Finned tube heat exchanger |
Experimental investigation on the air-side flow and heat transfer characteristics of 3-D finned tube bundle | |
Abstract The heat exchanger is widely applied to many thermal systems, and its structure significantly affects the flow and heat transfer characteristics. 3-D finned tube is a new type of carbon steel heat exchanger element that is low-fin-tube geometry with integral fins, which has larger heat transfer area and higher heat exchange efficiency. The current researches on the 3-D finned tube mainly focus on the flow and heat transfer performance of single tube by changing the structure parameters of fin or the condition of working medium. However, a reasonable tube bundle arrangement must be considered to obtain a compact structure in the engineering applications. So in the study, experiments are performed to investigate the air side flow and heat transfer characteristics of 3-D finned tube bundle with different geometries. The effects of varied transversal tube pitches, longitudinal tube pitches, and fin heights on Nu , Eu, and j/f are presented and discussed. The predictive correlations of 3-D finned tube bundle for Nu and Eu are proposed based on the presented data, and they can provide a theoretical reference for the industrial applications of 3-D finned tube. Finally, the flow and heat transfer characteristics of 3-D finned tube bundle are contrasted with those of other types of finned tube bundle from extant studies, and the results show that the 3-D finned tube bundle heat exchanger has higher air-side heat transfer performance and lower pressure drop. | |
03/01/2019 00:00:00 | |
Link to Article | |
4.2.6 | Finned tube heat exchanger |
Fin-tube heat exchanger performance for different louver angles | |
To choose the proper design for a heat exchanger in engineering industry and to evaluate the finned surface performance it is important to calculate fin efficiency. The heat transfer conditions, in tube-fin heat exchangers, can be modified for instance by changing the fin shapes. The angle of louver inclination affects the fluid flow direction and it has the effect on the heat transfer and temperature changes. In the paper, the heat transfer is estimated numerically for fins with and without louvers to choose the optimal louver angle in the car radiator. Numerical analyses are carried out to examine finned tube heat exchanger and to determine the performance of the radiator for eight different louver angles. Solutions are obtained by means of ANSYS program. The tube material is kept fixed as well as the heat exchanger fin and tube pitches (spacing) and the inlet air velocity. | |
01/01/2014 00:00:00 | |
Link to Article | |
4.2.7 | Finned tube heat exchanger |
Flow and heat transfer enhancement in tube heat exchangers | |
The performance of heat exchangers can be improved to perform a certain heat-transfer duty by heat transfer enhancement techniques. Enhancement techniques can be divided into two categories: passive and active. Active methods require external power, such as electric or acoustic field, mechanical devices, or surface vibration, whereas passive methods do not require external power but make use of a special surface geometry or fluid additive which cause heat transfer enhancement. The majority of commercially interesting enhancement techniques are passive ones. This paper presents a review of published works on the characteristics of heat transfer and flow in finned tube heat exchangers of the existing patterns. The review considers plain, louvered, slit, wavy, annular, longitudinal, and serrated fins. This review can be indicated by the status of the research in this area which is important. The comparison of finned tubes heat exchangers shows that those with slit, plain, and wavy finned tubes have the highest values of area goodness factor while the heat exchanger with annular fin shows the lowest. A better heat transfer coefficient ha is found for a heat exchanger with louvered finned and thus should be regarded as the most efficient one, at fixed pumping power per heat transfer area. This study points out that although numerous studies have been conducted on the characteristics of flow and heat transfer in round, elliptical, and flat tubes, studies on some types of streamlined-tubes shapes are limited, especially on wing-shaped tubes (Sayed Ahmed et al. in Heat Mass Transf 50: 1091–1102, 2014; in Heat Mass Transf 51: 1001–1016, 2015). It is recommended that further detailed studies via numerical simulations and/or experimental investigations should be carried out, in the future, to put further insight to these fin designs. | |
11/01/2015 00:00:00 | |
Link to Article | |
4.2.8 | Finned tube heat exchanger |
Influence of the degree of thermal contact in fin and tube heat exchanger: A numerical analysis | |
Abstract Present work aims to investigate the significance of thermal contact area between fins and tubes in a heat exchanger. The heat exchanger type selected for the study is a liquid-gas fin and tube heat exchanger. Four different cases namely I, II, III, and IV, based on a variable degree of thermal contact between fins and tubes are investigated. Case-I with 100% thermal contact area between the fin and tube is set as a reference to cases-II, III, and IV with a thermal contact area of approximately 70%, 50%, and 35%, respectively. Three-dimensional (3D) steady-state numerical models based on finite element method (FEM) are developed for the different cases studied. Conjugate heat transfer mechanism coupled with turbulent flow is simulated to elucidate temperature and velocity profiles. In order to develop a simplified model with desired physical phenomena, only gas-side flow over the fin is simulated in the present study. The performance of the heat exchanger is characterized in terms of overall heat transfer coefficient, Colburn j -factor, flow resistance factor, and efficiency index. Results obtained from numerical modeling are useful to examine the impact of the degree of thermal contact and to compare the performance of heat exchanger design in different cases. Comparative analysis indicates a significant influence of the degree of the thermal contact area between fin and tube on the overall performance. Case-I is found to have higher overall heat transfer coefficient of 47.332 W/(m 2 K), higher efficiency index of 9.131 and lower flow resistance factor of 0.123 among the cases investigated and highlights the need for perfect thermal contact between fin and tubes to meet the application based requirements. | |
08/01/2016 00:00:00 | |
Link to Article | |
4.2.9 | Finned tube heat exchanger |
Possibilities of Intensifying Heat Transfer in Heat Exchangers for High Temperature Applications | |
A high temperature heat transfer application actually represents the case of a heat exchanger operated within a process with high temperature. In every industrial domain, a different value of temperature may be considered “high”. We are active in the field of chemical, petrochemical, waste-to-energy, power and process energy recovery heat transfer applications. In these applications a tube-fin exchangers are successfully used for gas or liquid and/or aggressive fluids with temperatures up to 350 and/or 400 °C. They are also frequently used in combustion systems with air preheating applications. Tubular heat exchangers, especially those with U-tubes, helical and straight tubes are most frequently used for hightemperature applications with working temperatures above 650 °C. Extended surfaces are used as an intensification approach to decrease the area requirements on flue gas side. Selection of an extended surface depends on type of fuel. In the case of combustion of fuels producing flue gas with fouling tendency, studded tubes are preferred. More efficient finned tubes may be used if fuel burnt produces relatively clean flue gas. Generally enhanced surfaces are used for gaseous media with low heat transfer coefficient. Fins substantially enhance the heat transfer area and consequently heat duty of the equipment. Improving heat transfer performance is commonly referred to as heat transfer enhancement. Enhancement is usually represented by increasing the (film and overall) heat transfer coefficient by so called “passive” (surface extension) or “active” (increasing fluid turbulence) way. This paper presents a possible selection of novel types of longitudinally finned tubes intensifying the heat transfer utilizing both passive and active principles. It means that fins not only increase heat transfer area but also make the fluid flowing around fin to change the flow direction, i.e., to increase the turbulence. This allows increasing the film heat transfer coefficient on fin-side. | |
09/20/2013 00:00:00 | |
Link to Article | |
4.2.10 | Finned tube heat exchanger |
Research of Heat Exchanger with Multi Type Tubes and Its Application in Industry | |
The heat exchanger with multi type tubes is one new high efficiency heat exchanger.Currently,there is rare research focused on this king exchanger,and there is a less reported research on the feature of heat transfer for this exchanger.In this article, the primary research for this exchanger was carried out.With practical conditions in industrial constructions,tubular,multi type tubes and fin tube heat exchangers were compared in the properties of heat transfer and economy by using software HTRI.The pros of multi type tubes exchanger in industrial application were analyzed,by which references for the research and spreading of this kind of exchanger are provided. | |
01/01/2012 00:00:00 | |
Link to Article | |
4.3 Plate-fin-and-tube heat exchanger
The plate fin-and-tube heat exchangers are widely used in a variety of industrial applications, particularly in the heating, airconditioning and refrigeration, HVAC industries. There are many different types of geometry for heat exchangers available. Commonly they are composed of tubes, with plates perpendicular, resulting in a cross-flow profile as seen in the figure. There are different types of plate-fin geometry, the most common being the plain fin, where the fins are parallel plates attached to a hot element in the form of tubes or some other shape. These fins act as a sink, absorbing the heat out of the hot element with the help of conductive heat transfer. And then dissipating this absorbed heat onto the outside environment which is at a lower temperature. Art. [#ARTNUM](#article-26206-840680848)
There are numerous design options in this type of heat exchangers, as can be seen in the figure.
**Applications:**
* HVAC
* Refridgeration
4.3.1 | Plate-fin-and-tube heat exchanger |
---|---|
Performance Evaluation of Plate-Fin-And Tube Heat Exchanger with Wavy Fins- A Review | |
The plate fin-and-tube heat exchangers are widely used in variety of industrial applications, particularly in the heating, air-conditioning and refrigeration, HVAC industries. In most cases the working fluid is liquid on the tube side exchanging heat with a gas, usually air. It is seen that the performance of heat exchangers can be greatly increased with the use of unconventionally shaped flow passages such as plain, perforated offset strip, louvered, wavy, vortex generator and pin. The current study is focused on wavy-fin. The wavy surface can lengthen the path of airflow and cause better airflow mixing. In order to design better heat exchangers and come up with efficient designs, a thorough understanding of the flow of air in these channels is required. Hence this study focuses on the heat transfer and friction characteristics of the air side for wavy fin and tube heat exchanger. | |
01/01/2014 00:00:00 | |
Link to Article | |
4.4 Corrugated plate heat exchanger
The corrugated plate heat exchanger consists of a number of gasketed plates constrained between an upper carrying bar and a lower guide bar. The plates are compressed between the fixed frame and the movable frame by using many tie bolts. In addition to the plate efficiency, corrugation patterns that produce turbulent flows, it is not only cause's unmatched efficiency; it also produces a heat exchanger self-cleaning nature, which in turn reducing the fouling effect. There are several patterns possible on corrugated plates. Art.
[#ARTNUM](#article-26205-2561023270)
4.4.1 | Corrugated plate heat exchanger |
---|---|
Corrugated plate heat exchanger review | |
The developments and the enhancements in all the heat transfer equipments are mainly purposed for energy savings and savings in projects capital investment, through reducing the costs (energy or material). The better heat exchanger is one that transfer's high heat rate at low pumping power with a minimum cost. The spent of money for the research and development in corrugated plate heat exchangers, in last decades, from some companies, offered different and versatile types and models of that heat exchanger. In the current study I made a focus on researcher's efforts in research and developments for corrugated plate heat exchanger. This type of heat exchangers is widely used for different engineering fields and applications. Research reactors represent one of the important engineering fields that extensively use corrugated plate heat exchangers due to their simplicity in assembly/disassembly and their easy maintainability. The corrugated plate heat exchanger has a great flexibility than the other types of heat exchangers; both its heat transfer area and its cooling flow could be increased or decreased easily, so; it is commonly used for enlargement and upgrading works. The current revision incorporated different topics like; the plate heat exchanger structure, thermal performance, heat transfer enhancement mechanisms as well as plate heat exchanger advantages and limitations. The corrugated plate heat exchanger works efficiently in both single phase and two phase flow, while the two phase flow region still needs a lot of research work. Also; the corrugated plate heat exchanger thermal performance and pressure drop behaviours when using nano-fluids were discussed in the current revision. | |
04/01/2017 00:00:00 | |
Link to Article | |
4.5 Coil wired tube heat exchanger
To enhance the mixing in a tube, and therefore improve heat transfer a wired coil helical structure can be added to the tube. Art. [#ARTNUM](#article-26751-2519485646) The coil can induce an increased pressure drop, but reduce the fouling of the system.
4.5.1 | Coil wired tube heat exchanger |
---|---|
A comprehensive review on double pipe heat exchangers | |
Abstract Growing need to develop and improve the effectiveness of heat exchangers has led to a broad range of investigations for increasing heat transfer rate along with decreasing the size and cost of the industrial apparatus accordingly. One of these many apparatus which are used in different industries is double pipe heat exchanger. This type of heat exchanger has drawn many attentions due to simplicity and wide range of usages. In recent years, several precise and invaluable studies have been performed in double pipe heat exchangers. In this review, the development procedure that this type of heat exchanger went through has been analyzed in details and the heat transfer enhancement methods in aforementioned heat exchangers have also been widely discussed. Having also tried the best to present a comprehensive research, the authors gathered information regarding the usage of these methods such as active, passive and compound methods which is worth noting that the studies concerning using passive methods in double pipe heat exchangers have been frequently cited. Moreover, various studies concerning using nanofluids in double pipe heat exchangers have been discussed in details. In this review, correlations of mostly Nusselt number and pressure drop coefficient are also presented. It is believed that this review provides new insights for further investigations. | |
01/01/2017 00:00:00 | |
Link to Article | |
4.5.2 | Coil wired tube heat exchanger |
Turbulent flow heat transfer and fluid friction in helical-wire-coil-inserted tubes | |
Abstract Results are presented from experimental investigations of heat transfer in a 25 mm I.D. copper tube, tightly fitted with helical-wire-coil inserts of varying pitch ( p ), helix angle ( x ) and wire diameter ( e ). A similarity law approach was attempted to interpret the friction and heat transfer results and correlate them in terms of roughness Reynolds number ( h + ), momentum transfer roughness function R ( h + ) and heat transfer roughness function G ( h + , Pr ). The present results are compared with previously published results and a generalized correlation for the G -function has been developed, which is applicable for different types of rough surfaces. An optimization study was made on the basis of maximization of the heat transfer rate and also minimization of pumping power and heat exchanger frontal area to identify the most efficient tube within the matrix of data. | |
12/01/1983 00:00:00 | |
Link to Article | |
4.6 Twisted-tape tube heat exchanger
A twisted tape insert is one of the most efficient heat transfer enhancement methods which has a wide range of usages due to simplicity, low cost, easy instalment and routine maintenance. Generally, twisted tape performs as a continuous swirl generator which causes turbulence on flow.
The induced swirl on the tube side results in higher near-wall velocities. This leads to better mixing of the fluid which eventually results in a higher heat transfer rate. Art. [#ARTNUM](#article-26311-2519485646)
Twisted tape requires a reasonable high flow for the induced effect. This makes twisted tape most effective with turbulent flows with a limited pressure drop, while with laminar flow the improvement are limited. The twisted tape induces a higher pressure drop on the tube side.
Supplier
4.6.1 | Twisted-tape tube heat exchanger |
---|---|
A comprehensive review on double pipe heat exchangers | |
Abstract Growing need to develop and improve the effectiveness of heat exchangers has led to a broad range of investigations for increasing heat transfer rate along with decreasing the size and cost of the industrial apparatus accordingly. One of these many apparatus which are used in different industries is double pipe heat exchanger. This type of heat exchanger has drawn many attentions due to simplicity and wide range of usages. In recent years, several precise and invaluable studies have been performed in double pipe heat exchangers. In this review, the development procedure that this type of heat exchanger went through has been analyzed in details and the heat transfer enhancement methods in aforementioned heat exchangers have also been widely discussed. Having also tried the best to present a comprehensive research, the authors gathered information regarding the usage of these methods such as active, passive and compound methods which is worth noting that the studies concerning using passive methods in double pipe heat exchangers have been frequently cited. Moreover, various studies concerning using nanofluids in double pipe heat exchangers have been discussed in details. In this review, correlations of mostly Nusselt number and pressure drop coefficient are also presented. It is believed that this review provides new insights for further investigations. | |
01/01/2017 00:00:00 | |
Link to Article | |
4.6.2 | Twisted-tape tube heat exchanger |
Improving the performance of shell-and-tube heat exchangers by the addition of swirl | |
Heat exchanger is a component which is used to transfer the heat from one medium to another efficiently. Generally, they occupy a large space compared to other components and such bulky designs are not attractive in the modern industrial applications due to several constraints. Therefore, it is invaluable to develop compact heat exchangers but with the improved performance. In this work, an investigation was made on the possibility of reducing the size of a shell-and-tube heat exchanger by addition of swirl. Swirl was generated by using a twisted-tape which inserted inside tube and the effects of these tapes on the heat transfer rate and pressure drop were theoretically studied. The results showed that a half-length regular spaced twisted-tape insert gave the lowest Nusselt number while a full-length twisted-tape insert gave the maximum Nusselt number and hence the highest rate of heat transfer. The length of the heat exchanger could be reduced by 13.3% with a full-length twisted tape and this would be result in 6.8% of reduction of the fabrication cost. Therefore, addition of swirl into the fluid flow should help to design compact and low cost heat exchanges with improved performance but the pressure drop increased leading to an increase of the required pumping power. A prototype shell-and-tube heat exchanger was designed and fabricated based on the theoretical results. Studies are underway to experimentally investigate the overall effectiveness of the use of twisted-tape inserts for enhancing the heat transfer rate by considering all the related benefits and drawbacks. | |
01/01/2014 00:00:00 | |
Link to Article | |
4.7 Rotor enhanced shell and tube
In order to improve heat transfer efficiency and solve the fouling problem, a new type of heat exchanger whose tube inserted with plastics rotors was designed in the study. Art. [#ARTNUM](#article-26249-2141855446)
A rotor enhanced shell and tube can be used when fouling is a huge problem. To boost the heat transfer the fluid velocity should be above the critical velocity. This is depended on the size and amount of rotors.
Not commercially applied.
4.7.1 | Rotor enhanced shell and tube |
---|---|
Research on enhanced heat transfer characteristics in heat exchanger inserted with rotors | |
Shell and tube heat exchanger is an important process device in high-energy industry. In order to improve heat transfer efficiency and solve the fouling problem, a new type heat exchanger whose tube inserted with plastics rotors was designed in the study. Furthermore, theoretical analysis and experimental validation were performed for the exchanger inserted with 19–100 and 19–400 specification rotors respectively. The results showed that heat exchangers whose tube inserted with 19–400 specification rotors obtained better performance. In addition, it is found that 19–100 specification rotors exist critical velocity. When flow velocity is greater than the critical velocity, the heat exchanger shows better heat transfer performance than the smooth tube. Moreover, the flow rate of heat exchanger whose tube inserted with different rotors was optimized, when the inlet temperature of hot water was constant. These findings provide a basis in understanding of heat exchanger inserted with rotor. | |
04/01/2011 00:00:00 | |
Link to Article | |
4.8 Metal foam heat exchangers
Opencell porous metal foams have received attention for use in compact heat exchangers due to their increasing availability and improved thermal performance. In recent years, considerable research has been conducted on use of metallic and nonmetallic foams to further improve performance of stateoftheart heat exchangers. Art. [#ARTNUM](#article-27304-2070465275). They can be used as an enhancement in plate or tube heat exchangers, as shell-filling material or plate material (see pictures).
**Research findings:**
* In this paper, open-cell aluminum foam is considered as a highly compact replacement for conventional louver fins in brazed aluminum heat exchangers. Art. [#ARTNUM](#article-27304-1996174950)
* The heat exchanger performance is one of the main contributors to the thermodynamic and cost effectiveness of the entire LNG regasification system. Within the paper, the authors discuss a new concept for a compact heat exchanger with a micro-cellular structure medium to minimize volume and mass and to increase thermal efficiency. Numerical calculations have been conducted to design a metal-foam filled plate heat exchanger and a shell-and-tube heat exchanger using published experimental correlations. The results show that the metal-foam plate heat exchanger has the best performance at different channel heights and mass flow rates of fluid. In the optimized configurations, the metal-foam plate heat exchanger has a higher heat transfer rate and lower pressure drop than the shell-and-tube heat exchanger as the mass flow rate of natural gas is increased. Art. [#ARTNUM](#article-27304-2196335867)
**Applications:**
Enhanced heat exchangers in:
* LNG plants
* aerospace
* electronics
* automotive
4.8.1 | Metal foam heat exchangers |
---|---|
A Comparison of Metal-Foam Heat Exchangers to Compact Multilouver Designs for Air-Side Heat Transfer Applications | |
High-porosity metal foams, with novel thermal, mechanical, electrical, and acoustic properties, are being more widely used in various industrial applications. In this paper, open-cell aluminum foam is considered as a highly compact replacement for conventional louver fins in brazed aluminum heat exchangers. A model based on the ϵ-NTU method is developed to compare the flat-tube, serpentine louver-fin heat exchanger to the flat-tube metal-foam heat exchanger. The two heat exchangers are subjected to identical thermal-hydraulic requirements, and volume, mass, and cost of the metal-foam and louver-fin designs are compared. The results show that the same performance is achieved using the metal-foam heat exchanger but a lighter and smaller heat exchanger is required. However, the cost of the metal-foam heat exchanger is currently much higher than that of the louver-fin heat exchanger, because of the high price of metal foams. If the price of metal foam falls to equal that of louver-fin stock (per unit mass), t... | |
01/01/2012 00:00:00 | |
Link to Article | |
4.8.2 | Metal foam heat exchangers |
Application of metal foam heat exchangers for a high-performance liquefied natural gas regasification system | |
The intermediate fluid vaporizer has wide applications in the regasification of LNG (liquefied natural gas). The heat exchanger performance is one of the main contributors to the thermodynamic and cost effectiveness of the entire LNG regasification system. Within the paper, the authors discuss a new concept for a compact heat exchanger with a micro-cellular structure medium to minimize volume and mass and to increase thermal efficiency. Numerical calculations have been conducted to design a metal-foam filled plate heat exchanger and a shell-and-tube heat exchanger using published experimental correlations. The geometry of both heat exchangers was optimized using the conditions of thermolators in LNG regasification systems. The heat transfer and pressure drop performance was predicted to compare the heat exchangers. The results show that the metal-foam plate heat exchanger has the best performance at different channel heights and mass flow rates of fluid. In the optimized configurations, the metal-foam plate heat exchanger has a higher heat transfer rate and lower pressure drop than the shell-and-tube heat exchanger as the mass flow rate of natural gas is increased. | |
06/01/2016 00:00:00 | |
Link to Article | |
4.8.3 | Metal foam heat exchangers |
Application of Metal Foams for Improving the Performance of Air-Cooled Heat Exchangers | |
This thesis investigates the application of metal foam heat exchangers to the air-cooled condensers of geothermal power plants in Australia where the resources are mostly located at the arid areas where there is no water for evaporative cooling of the power plant. One way to remove the heat from the thermodynamic cycles is to use (the most common) finned-tube heat exchangers, consisting of tubes with external fins to increase the air-side heat exchange surface. Another possible alternative is a class of designed porous materials called metal foams, containing such advantages as low-density, high area/volume ratio, and high strength structure. Therefore, they have been applied in a variety of industrial. The numerical study, in three main sections, has been conducted to explore that possibility. First, a comparison between the performance of a metal foam-wrapped solid cylinder in cross-flow and a commercially available finned-tune heat exchanger is investigated. Effects of the key parameters including the free-stream velocity and characteristics of metal foam such as porosity, permeability, and form drag coefficient on heat and fluid flow are examined. Being a determining factor in pressure drop and heat transfer increment, the porous layer thickness is changed systematically to observe that there is an optimum layer thickness beyond which the heat transfer does not improve while the pressure drop continues to increase. This has been verified by the application of Bejan’s Intersection of Asymptotes method. Results have been compared to those of a finned-tube heat exchanger to observe a higher area goodness factor for metal foam-wrapped cylinder. In the second part, an optimization study is carried out to discover an optimized design of metal foam heat exchangers as replacements for finned-tubes in air-cooled condensers of a geothermal power plant. Two different optimization techniques, based on first and second law (of thermodynamics) are reported. While the former leads to the highest heat transfer rate with as low pressure drop as possible, the latter minimizes the generated entropy in the thermodynamic system. Interestingly the two methods lead to the same optimal design. The new design has been compared to the conventional air-cooled condenser designed and optimized by using the commercially available software ASPEN. It is shown that while the heat transfer rate increases significantly (by an order of magnitude) compared to the finned tube for the same main flow obstruction height, the pressure drop increase is within an acceptable range. Further comparison between the two systems are carried out, making use of Mahjoob and Vafai's performance factor developed specifically for metal foam heat exchangers. Following that, the third part explores the heat transfer from a metal foam-wrapped tube bundle. Effects of key parameters, including the free stream velocity, longitudinal and transversal tube pitch, metal foam thickness and characteristics of the foam on heat and fluid flow are examined. It can be observed that the performance of the metal foam heat exchangers, measured in terms of area goodness factor, can be about four times better than that of the conventional design of finned-tube heat exchangers. It is also found that even a very thin layer of metal foam, when wrapped around a bare tube bundle, can significantly improve the area goodness factor. Finally, it is shown that while friction factor is more sensitive to the metal foam permeability than its porosity, the converse is true when it comes to the Colburn factor. | |
04/01/2011 00:00:00 | |
Link to Article | |
4.8.4 | Metal foam heat exchangers |
Foam Heat Exchangers: A Technology Assessment | |
Open-cell porous metal foams have received attention for use in compact heat exchangers due to their increasing availability and improved thermal performance. In recent years, considerable research has been conducted on use of metallic and nonmetallic foams to further improve performance of state-of-the-art heat exchangers. In this paper, we report preliminary results from fabrication, development and experimental investigation of thermal-hydraulic performance of high-temperature metal foam heat exchangers for automotive exhaust gas recirculation (EGR) system. A brief review of nickel–chromium and stainless-steel foam heat exchanger technology and of recent efforts on their manufacturing techniques for a liquid-to-air heat exchange application is presented. Measured heat transfer and pressure drop data for foam heat exchangers and their comparison with performance of a conventional wavy plate-fin heat exchanger are discussed. Technical challenges and risks associated with foam heat exchangers are discusse... | |
01/01/2012 00:00:00 | |
Link to Article | |
5. Regenerative
BackA regenerative heat exchanger, or more commonly a regenerator, is a type of heat exchanger where heat from the hot fluid is intermittently stored in a thermal storage medium before it is transferred to the cold fluid. To accomplish this the hot fluid is brought into contact with the heat storage medium, then the fluid is displaced with the cold fluid, which absorbs the heat.
5.1 Fixed matrix heat exchanger
In a fixed matrix regenerator, a fluid moves through a fixed bed, storing its heat in one direction. When the flow is reversed, another (or the same) fluid can take up this heat again. Phase transitions can also be used, but gas-gas heat exchange is more common.
**Applications:**
* HVAC
* Steel industry
* Glass industry
* Waste heat recovery
* Power plants
5.1.1 | Fixed matrix heat exchanger |
---|---|
A criterial analysis of the effectiveness of air-to-air heat exchangers with periodic change of airflow direction | |
Abstract The physico-mathematical model of the regenerative heat exchanger with periodic changes of air flow direction has been developed. The model takes into account phase transitions both on the surface of air channels of heat exchange matrix and directly in the airflow. In this paper, the results of the influence of parameter groups on the heat exchanger effectiveness are generalized. Such generalization is reached by identifying the governing dimensionless groups in the system of equations. The analysis using the generalized parameters allows considerably simplifying the study of processes with a large number of parameters. In addition, the influence of air humidity and temperature on the sensible and latent effectiveness of the heat exchanger has been analyzed. Computations enable determining the heat exchange matrix material that is the most suitable in terms of its thermophysical properties. | |
02/01/2018 00:00:00 | |
Link to Article | |
5.1.2 | Fixed matrix heat exchanger |
CFD Model of Regenerative Heat Exchanger | |
This paper is focused on the Computational fluid dynamics (CFD) modeling of regenerative heat exchanger suitable for animal houses. Buildings used for housing of animals in farms with intensive breeding, like poultry or pig houses, are characterized by high generation of heat inside, partly produced by animals, and in the case of small young animals, supplemented also by heating. On the other side these buildings need intensive ventilation which causes big losses of energy by exhausted air. A good way how to reduce heat losses can be the use of technical systems of heat recovery. There are two principal constructions of heat exchangers for heat recovery. There are either recuperative or regenerative heat exchangers. Industrially produced heat exchangers, commonly used in residential or industrial buildings, can be used in agricultural conditions only with difficulties, mainly because of the high dust concentration, which is extremely high in animal houses. The methods of CFD modeling were used to calculate main parameters of special heat exchanger, developed for application in animal houses. The construction of regenerative heat exchanger with fixed matrix is based on heat accumulation in material of matrix in the form of massive plates. The program Fluent was used for airflow and heat exchange simulations. Results of simulations were verified by measurement of prototype of real heat exchanger. | |
04/26/2015 00:00:00 | |
Link to Article | |
5.1.3 | Fixed matrix heat exchanger |
EXERGY LOSS ANALYSIS OF REGENERATIVE SYSTEM OF ONE 660 MW UNIT BASED ON MATRIX METHOD | |
Based on the structure and parameters of the regenerative system for one 660 MW unit,the matrix equation of exergy loss distribution has been given.Selecting operating condition point under 100%,75%,50%,and 30% load,the exergy loss and exergy efficiency of regenerative heater has been calculated.The calculation and analysis show that the heat exchange coefficient must try to be increased for reducing the temperature difference of heat exchange at certain heat transfer and heater structure,including decrease of valve resistance,and enhance of working medium flow speed,etc. | |
01/01/2011 00:00:00 | |
Link to Article | |
5.1.4 | Fixed matrix heat exchanger |
Influence of condensation on the efficiency of regenerative heat exchanger for ventilation | |
The paper presents a physical and mathematical model for calculating the air-to-air heat exchanger with periodically changing direction of the air flow. It accounts for vaporization and condensation on the channel walls of the heat exchange matrix with regular structure as well as possible formation of water fog directly in the air flow. The model can be used to analyze the influence of operating parameters, the geometric dimensions of the channels and properties of the used materials on the work efficiency of the heat exchanger. The results of calculations of the influence of indoor air humidity on heat and moisture transfer processes in the regenerative heat exchanger are provided. Sensible and latent efficiency of the regenerative heat exchanger as well as their dependence on relative humidity of indoor air are determined. The relationship between the outdoor air temperature and relative humidity of indoor air, at which ice formation begins in the channels of the heat exchange matrix, is found. | |
01/01/2017 00:00:00 | |
Link to Article | |
5.2 Rotary heat exchanger
Rotary heat exchangers or heat wheels are popularly used for heat recovery in many industrial and domestic applications. Art. [#ARTNUM](#article-26250-2790684841). They employ rotary 'heat-storing elements' that rotate between cold and hot streams to exchange heat.
The rotor consists of a large scale of heat transfer plates known as the matrix. The matrix can be made of steel, ceramics, glass and plastic. The rotor rotates continuously with a constant fraction of the core in the flue gas stream and the remaining fraction in the cooling air stream. The saturated wet flue gas is cooled by the matrix, and the water vapour is condensed on the wall of the matrix as the decrease in temperature of flue gas. Art. [#ARTNUM](#article-26250-2902036760)
Different type of rotors is available for different purposes. The condensation film which has an aluminium film. This rotor is used for recovering heat or cold from the ambient air. The enthalpy rotors have a hygroscopic surface which supports the heat transfer of moisture. The sorption rotors consisting of a zeolite coating, maximizing heat transfer and moisture all year long especially in warm and humid climates. The epoxy rotor is an epoxy-coated aluminium which offers high corrosion protection. Optimal for envierments where the air can be corrosive used for the heat transfer.
The rotors are able to handle airflow from 1000 m³/hr to 150000 m³/hr. The heat transfer efficiency goes up to 85% and the system is frost resistant up to -15 °C.
**Applications:**
* HVAC (very common)
* Waste heat recovery (common)
* Shipping
* Chemical plants
* Power plants
* Air/gas handling
5.2.1 | Rotary heat exchanger |
---|---|
A method is presented for studying heat transfer using the optimization of param- eters, realized in a study of heat exchange with a rotating cylindrical surface. | |
Heat exchangers with rotating heat-transfer devices are beginning to be introduced in many branches of industry, such as the power, chemical, and automotive industries [1-3]. The use of such heat exchangers for the heating and cooling of liquids seems advisable because of the possibility of considerable intensification of heat transfer from both sides of a rotating wall [2, 4]. In addition, for rotating elements it is easier to provide conditions under which contamination of the surface is inhibited or entirely absent [5-7], whereas the latter is considered to be a main problem in heat transfer [8-10]. The planning of such heat exchangers is difficult, however, because of the absence of sufficiently reliable information on heat transfer in channels which differ in numerous structural properties. The design of an experimental rotary heat exchanger and a diagram of the experimental installation are shown in Fig. i. The heat exchanger is intended predominantly for the cooling of viscous liquids and saturated solutions and consists of a hollow cylinder rotating coaxially in a frame with longitudinal perforated ribbing. One or two built-in pumps are mounted at the ends of the cylinder for the pumping of liquid through the annular channel and the prevention of leakage through the upper sealing unit. Since the rotation stabilizes the flow within the cylinder, a perforated wall for the distribution of the heat-transfer agent over the inner surface of the cylinder and a false bottom for bringing it out near the cylindrical surface are mounted in the cylinder in order to intensify the heat transfer. Film flow of the heat-transfer agent exists due to the false bottom in the cylinder, with the film being continuously turbulized by jets which uniformly bathe the heat-transfer surface. The heat exchanger investigated had the following dimensions: r' = 0.06475 m, b = 0.02425m, I=0.498m; gap between edges of ribbing and cylinder 0.1b; ribbing perforatio~ 38.5%; gap between rim of false bottom and inner surface of cylinder 0.002 m; thickness of heat-transfer wall 0.00295 m. The performated wall was made with 234 openings arranged uniformly in staggered order in 39 rows, and the distance from the points of discharge of the jets to the surface was 0.0238 m. The heat-transfer agent was distributed within the cylinder as follows: 10% of the entire flow entered in the top section, creating a stable film, while the remaining flow was distributed over 222 openings, the diameters of which were calculated from the condition of uniform distribution. Heat exchange in a smooth annular channel containing an inner rotating cylinder has been studied by many authors, a basic list of whom is presented in the monographs [i, 2, ii, 12]. Heat transfer through the annular gap from the wall of the rotating cylinder (or the other way) in the absence of an axial stream is studied in the majority of the works. Few experimental studies have been conducted with a determination of the heat-transfer coefficients and in the presence of an axial stream [3, 4, 13, 14]. The procedure of intensification of the heat exchange by installing longitudinal (unperforated) ribbing on the wall of the stationary cylinder was studied in [4]. Generalizing data are not obtained by the author, however. Data on the intensification of heat transfer using the jet-film motion described above are absent from the literature. | |
01/01/1976 00:00:00 | |
Link to Article | |
5.2.2 | Rotary heat exchanger |
A novel design of rotary regenerative condensing heat exchanger for the dehydration from high humidity flue gas | |
Abstract A rotary regenerative condensing heat exchanger was proposed for dehydration of the flue gas outflowing from the desulfurization tower in coal-fired power plant. An analytical model of heat and mass transfer processes in the regenerative condensing heat exchanger was developed. A calculation program was built by using an iterative solution technique to compute the heat transferred from flue gas to cooling air and the condensation rate of water vapor in the flue gas. The distributions of flue gas temperature, matrix temperature, water vapor mass fraction and condensate water mass were analyzed. The effects of matrix materials, operational and structural parameters of the rotor on the condensation efficiency were examined. The condensation efficiency from high to low for different matrix materials are in the sequence: SiC ceramic > carbon steel > fluorine plastic > Borosilicate Glass. Once the rotation speed, the height and radius of the rotor are larger than specific values, their changes are less effective on the condensation efficiency. Compared with the fluorine plastic tube condensing heat exchanger, the rotary regenerative condensing heat exchanger was more effective and economical on the whole volume and the capital cost to meet the same requirement of condensation efficiency. | |
03/01/2019 00:00:00 | |
Link to Article | |
5.2.3 | Rotary heat exchanger |
A simple effectiveness model for heat wheels | |
Abstract Rotary heat exchangers or heat wheels are popularly used for heat recovery in many industrial and domestic applications. In this study, a simple effectiveness model is developed for general use in the field. Firstly, approximate solution is obtained for the governing equations of a periodic-flow heat exchanger by assuming similarity with a steady-state heat exchanger and then used to derive an effectiveness correlation. The correlation is compared with a widely accepted reference in the literature and found to give a maximum error of 5% in the investigated ranges. Simple empirical correlations are also provided for practical use in the field. | |
05/01/2018 00:00:00 | |
Link to Article | |
5.2.4 | Rotary heat exchanger |
Air-cooled heat exchanger applied to external rotary kiln wall in forced and natural draft | |
Abstract The present paper deals with experimental measurements performed within a heat exchanger devoted to the thermal rotating machineries. The device is based on a rotor-stator system scaled from an industrial rotary kiln. The thermal recovery system is able to capture the heat losses while the kiln wall is cooled. The inner moving wall-to-air heat exchanges measured through the insulated external shell are compared to the values established in various flow conditions similar to the present geometry. The thermal convection regimes are distinguished according to the different forces exerted on the fluid air motion: the buoyancy forces being compared to the inertial effects combining the centrifugal and the axial motions. General scaling relationships devoted to the natural, mixed and forced convection regimes are proposed in an extended range of the Richardson numbers. | |
12/01/2017 00:00:00 | |
Link to Article | |
5.2.5 | Rotary heat exchanger |
Visual experimental study on residence time of particle in plate rotary heat exchanger | |
Abstract The plate rotary heat exchanger (PRHE) was developed as a new type of heat transfer equipment applied in coal moisture control (CMC) industrial process. Being an important factor during the producing process, the mean residence time (MRT) of particles inside PRHE was investigated. Visual experiments on MRT were carried out under identical filling degree ( f = 10%), while the particle flow rate, rotating speed and inclination of PRHE were varied. A Perspex rotary drum was used with an inner diameter of 300 mm and a length of 1000 mm. Eight rectangular plates were designed as the “heating plates”. Two different types of particles were utilized as experimental materials. The results indicated that MRT decreased with the increments of particle flow rates, rotating speed and inclination of PRHE. Compared with particle flow rate, the variable of MRT was sensitive to the increasing of rotating speed and PRHE slope, especially when the rotating speed was low. And the distribution of MRT was similar ideally normal. Then, based on the experimental results two empirical correlations were regressed by least square method, both of the two correlations were valid under most of the conditions and the mean deviations in MRT prediction were 8.1% and 8.0% respectively. | |
01/01/2017 00:00:00 | |
Link to Article | |
5.3 Rotating hood regenerator
In a rotating hood regenerating, the heat storage elements are stationary, while the elements through which the fluids flow rotate. In principle, it is the opposite of a rotary heat exchanger. It is also called a Rothemühle.
**Patent findings:**
Regenerative heat exchanger for heating > =2 parallel air or gas streams consists of a rotating hood over a fixed chamber of solid material for heat retention. The hood is one of a pair above and below the chamber and is divided into >=2 sections either side of a central axis. The flow area of each pair of sections is the same. These radiate from the centre where there are several concentric ducts for the various parallel gas or air streams. The hood and the central ducts are sealed from the hot exhaust gas flowing outside the hood by flexible seals. These are held in position by springs the tension of which can be adjusted. The device is of use in recovering heat from an exhaust gas stream where two or more temp. controlled air streams are required e.g. for preheating prim. and sec. air. Pat. [#ARTNUM](#article-26253-2875827312)
**Applications:**
* HVAC
* Exhaust gas heat recovery
* Air preheater
Supplier
5.3.1 | Rotating hood regenerator |
---|---|
Regenerative heat exchange for two air streams - having rotating hood divided into several sections | |
Regenerative heat exchanger for heating >=2 parallel air or gas streams consists of a rotating hood over a fixed chamber of solid material for heat retention. The hood is one of a pair above and below the chamber and is divided into >=2 sections either side of a central axis. The flow area of each pair of sections is the same. These radiate from the centre where there are several concentric ducts for the various parallel gas or air streams. The hood and the central ducts are sealed from the hot exhaust gas flowing outside the hood by flexible seals. These are held in position by springs the tension of which can be adjusted. Device is of use in recovering heat from an exhaust gas stream where two or more temp. controlled air streams are required e.g. for preheating prim. and sec. air. | |
06/08/1977 00:00:00 | |
Link to Article | |
5.3.2 | Rotating hood regenerator |
Regenerative heat exchanger for gases - having rotating hood over fixed heat transfer elements with common chamber below | |
Gases are processed in equipment provided with a regenerative heat exchange section which can be used to preheat or cool gas before it enters the process section. The heat exchange matrix with its associated processing sections is divided radially into a number of compartments, above which is a rotating hood which serves as a gas inlet or outlet compartment fed from a central duct. The other gas branch is the shell of the vessel and surrounds. A chamber below the processing zone serves as a common chamber for gas flow between the two zones as well as for collecting other products of the processing zone. The appts. may be used in all applications where processing a gas implies a temp. change. Gas flow can be in either direction. | |
05/28/1975 00:00:00 | |
Link to Article | |
5.4 Microscale regenerative heat exchanger
When a hot fluid flows through the cell, heat from the fluid is transferred to the cell walls and stored there. When the fluid flow reverses direction, heat is transferred from the cell walls back to the fluid. It has a multilayer grating structure in which each layer is offset from the adjacent layer by half a cell which has an opening along both axes perpendicular to the flow axis. Each layer is a composite structure of two sublayers, one of a high thermal conductivity material and another of a low thermal conductivity material. [\[Wiki\]](https://en.wikipedia.org/wiki/Regenerative_heat_exchanger)
A micro-scale regenerator has been designed, analytically optimized, and fabricated. The regenerator composed of multiple layers of photoresist-nickel structure in an offset grating pattern. The offset pattern and composite structure minimizes axial conduction losses and disrupts boundary layer formation for improved heat transfer. Art. [#ARTNUM](#article-26764-1997390424)
The microscale regenerative heat exchanger is being developed for application in a micro-Stirling engine.
5.4.1 | Microscale regenerative heat exchanger |
---|---|
Micro-Scale Regenerative Heat Exchanger | |
A micro-scale regenerative heat exchanger has been designed, optimized and fabricated for use in a micro-Stirling device. Novel design and fabrication techniques enabled the minimization of axial heat conduction losses and pressure drop, while maximizing thermal regenerative performance. The fabricated prototype is comprised of ten separate assembled layers of alternating metal-dielectric composite. Each layer is offset to minimize conduction losses and maximize heat transfer by boundary layer disruption. A grating pattern of 100 micron square non-contiguous flow passages were formed with a nominal 20 micron wall thickness, and an overall assembled ten-layer thickness of 900 microns. Application of the micro heat exchanger is envisioned in the areas of micro-refrigerators/coolers, micro-power devices, and micro-fluidic devices. | |
11/01/2004 00:00:00 | |
Link to Article | |
6. Direct contact
BackDirect contact heat exchangers involve heat transfer between hot and cold streams of two phases in the absence of a separating wall. Thus such heat exchangers can be classified as:
* Gas – liquid
* Immiscible liquid – liquid
* Solid-liquid or solid – gas
Most direct contact heat exchangers fall under the Gas – Liquid category, where heat is transferred between a gas and liquid in the form of drops, films or sprays.
6.1 Gas-solid heat exchangers
Gas-solid heat exchange is facilitated by bed-type heat exchangers, most commonly by solid granules forming a bed. Moving beds, fluidized beds and conveyor belts are examples.
6.1.1 | Gas-solid heat exchangers |
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Engineering design of direct contact counter current moving bed heat exchangers | |
Abstract A heat transfer model was applied to simulate heat exchange in a direct contact counter current moving bed (CCMB) heat exchanger associated with a dry slag granulation process developed by CSIRO. Cold air is used to recover heat from hot solid slag granules in the heat exchanger. Experimental data was used to calibrate the heat transfer model. The model was then used to predict the solid and gas temperature distributions along the height of the bed, the heat loss, and the operating and design conditions for scale-up of the CCMB to semi-industrial and industrial operations. Two scenarios were examined using the model to determine conditions for i) minimising the solid outlet temperature and ii) maximising the gas outlet temperature. The model can also be used to determine the nominal bed height to ensure that the designed gas outlet temperature is achieved. The modelling results suggest that a relatively small bed height (below 0.5 m) will be sufficient for heat exchange. The model also suggests that a solid to gas mass flow rate ratio of 0.8 should be used to minimise the solid outlet temperature, while a ratio of 1.0 should be used to maximise the gas outlet temperature. Therefore an appropriate operating window for a CCMB heat exchanger for recovering heat from hot slag was found with a solid to gas mass flow rate ratio between 0.8 and 1. | |
09/01/2015 00:00:00 | |
Link to Article | |
6.2 Spray column
A spray tower (or spray column or spray chamber) is a gas-liquid contactor used to achieve mass and heat transfer between a continuous gas phase (that can contain dispersed solid particles) and a dispersed liquid phase. It consists of an empty cylindrical vessel made of steel or plastic, and nozzles that spray liquid into the vessel. The inlet gas stream usually enters at the bottom of the tower and moves upward, while the liquid is sprayed downward from one or more levels. This flow of inlet gas and liquid in opposite directions is called countercurrent flow. [\[Wiki\]](https://en.wikipedia.org/wiki/Spray_tower)
Spray towers can handle flue gas streams up to 200000 m³/hr. The spray tower can be used as scrubber, particle separation and the chemical absorption of harmful substances. Cooling towers also use a spray-type system.
The system is highly resistant to fouling, with having little maintenance. Vapours up to 1300 °C can be cooled and scrubbed in one process. Separation degrees up to 98% per scrubber stage are possible with particles as small as 5 µm.
The gas and liquid requires to be separted afterwards, this is mostly done with a centrifugal separator.
**Applications:**
* Oil and gas
* Petrochemical & chemical
* Metallurgy
* Power plant
* Spray towers are usually applied for separation and scrubbing.
6.3 Tray column
A plate column (or tray column) is a piece of chemical equipment used to carry out unit operations where it is necessary to transfer mass between a liquid phase and a gas phase. In other words, it is a particular gas-liquid contactor. The peculiarity of this gas-liquid contactor is that the gas comes in contact with liquid through different stages; each stage is delimited by two plates (except the stage at the top of the column and the stage at the bottom of the column). [\[Wiki\]](https://en.wikipedia.org/wiki/Plate_column)
Different types of tray columns exist, such as disk and donut, sieve trays etc. Specific tray packings are chosen to enhance mass and heat transfer. Tray column can be as large as 4 m in diameter.
Usually used for liquid-liquid or gas-liquid contacting, or distillation.
**Applications:**
* Distillation
* Extraction
* Food and beverage
* Oil and gas
* (Petro)chemical
6.4 Bubble column
A bubble column reactor is an apparatus used to generate and control gas-liquid chemical reactions. It consists of a vertically-arranged cylindrical column filled with liquid, at the bottom of which gas is inserted. [\[Wiki\]](https://en.wikipedia.org/wiki/Bubble_column_reactor)
A bubble column used in:
* Petrochemical industries
* Biochemical industries
* Chemical industries
* Metallurgy
* Reactor, stripper, absorber
Suppliers
7. Compact
BackCompact heat exchangers are becoming increasingly important elements in many industrial processes, both in their original role as contributors to increased energy efficiency, and more recently as the basis for novel ‘intensified' unit operations.
7.1 Microchannel heat exchanger
Microchannels (broadly ⩽1 mm) represent the next step in heat exchanger development. They are a particular target of research due to their higher heat transfer and reduced weight as well as their space, energy, and materials savings potential over regular tube counterparts. Art. [#ARTNUM](#article-26150-2083412469). Microchannel heat exchangers can be used for many applications including high-performance aircraft gas turbine engines, heat pumps and air conditioning. Multiple materials are possible, resulting in high corrosion resistance when needed.
Microchannel heat exchangers can be produced in the same way as printed circuits, through etching and diffusion bonding. Art. [#ARTNUM](#article-26150-2475723589)
Machining of thin metal foils with specially contoured diamond cutting tools allows the production of small and very smooth fluid microflow channels for micro heat exchanger applications. Heat exchanger plate wall thickness, as well as fin dimensions, can be carefully controlled and machined to dimensions on the order of tens of micrometres. The plates are stacked and bonded with the vacuum diffusion process to form a crossflow, plate-type heat exchanger. Art. [#ARTNUM](#article-26150-2077945856)
The compactness of a microchannels heat exchanger can reduce the refrigerant charge by 30-60% under the same conditions as a fin and tube heat exchanger. While achieving an efficiency increase of 10-40%. The small size makes it easy to clean an dthe air side pressure drop is low.
Two-phase systems are possible.
**Applications:**
* Automotive
* Residential
* Electronics
* Power plants
* Process industry
* HVAC
7.1.1 | Microchannel heat exchanger |
---|---|
A review on microchannel heat exchangers and potential applications | |
Energy conversion and utilization are continuous but ever increasing processes for sustainability and economic development. Environmental concerns, such as thermal and air pollution, have dictated the practices of energy conservation and recovery, as well as the implementation of clean energy sources. Heat exchangers are an important component for processes where energy conservation is achieved through enhanced heat transfer. Such issues as increased energy demands, space limitations, and materials savings have highlighted the necessity for miniaturized light-weight heat exchangers, which provide high heat transfer for a given heat duty. However, while traditional heat exchangers employ conventional tubes (⩾6 mm) with various cross-sections, orientations, and even the enhanced surface textures, the technology is nearing its limits. Microchannels (broadly ⩽1 mm) represent the next step in heat exchanger development. They are a particular target of research due to their higher heat transfer and reduced weight as well as their space, energy, and materials savings potential over regular tube counterparts. In contrast to traditional tube heat exchangers, the heat transfer and fluid flow correlations, and the systematic design procedures are not yet well established for microchannels. It remains to be established whether the classical fluid flow and heat transfer theories and correlations are valid for microchannels. Numerous investigations are underway with researchers consolidating evidence on both sides of this question. This paper surveys the published literature on the status and potential of microchannels, and it identifies research needs, and defines the scope for long-term research. Based on results from the review, an air-to-liquid crossflow experimental infrastructure has been developed and commissioned. It will be used to investigate the heat transfer and fluid flow for a variety of working fluids in different microchannel test specimens. Further information and the heat balance status of the developed test facility are also presented. Copyright © 2010 John Wiley & Sons, Ltd. | |
06/10/2011 00:00:00 | |
Link to Article | |
7.1.2 | Microchannel heat exchanger |
Compact type micro-channel bending flat pipe heat exchanger | |
The invention discloses a compact type micro-channel bending flat pipe heat exchanger; a micro-channel bending flat pipe forms a heat exchanging core body, wherein one end is spliced to the left end of a flow collecting pipe and the other end is spliced to the right end of the flow collecting pipe; the upper part of the heat exchange core body is a condenser while the lower part is an evaporator; a fin is arranged in the micro-channel bending flat pipe of the condenser; heat conducting grooves corresponding to the micro-channel bending flat pipe are arranged on inside faces of a front heat conducting plate and a back heat conducting plate in the evaporator; the micro-channel bending flat pipe after buckling the front heat conducting plate with the back heat conducting plate is arranged in the heat conducting grooves of the front and back heat conducting plates and brazed together; through the front and back heat conducting plates, the heat is transferred to the micro-channel bending flat pipe in the evaporator; after heat absorption and vaporization of a cold media, the hot source is flowed to the condenser along with the flat pipe, air in the condenser takes away heat in the cold media; the cold media is liquefied and downwards flowed to the evaporating part along with the flat pipe; the process is repeated. The compact type micro-channel bending flat pipe heat exchanger is compact in structure, small in appearance volume, and can be widely applied to the place of which radiating load is small in industrial cooling, and the installation space is concentrated on one plane. | |
02/22/2017 00:00:00 | |
Link to Article | |
7.1.3 | Microchannel heat exchanger |
Diffusion-Welded Microchannel Heat Exchanger for Industrial | |
The goal of next generation reactors is to increase energy efficiency in the production ofelectricity and provide high-temperature heat for industrial processes. The efficient trans-fer of energy for industrial applications depends on the ability to incorporate effectiveheat exchangers between the nuclear heat transport system and the industrial process.The need for efficiency, compactness, and safety challenge the boundaries of existingheat exchanger technology. Various studies have been performed in attempts to updatethe secondary heat exchanger that is downstream of the primary heat exchanger, mostlybecause its performance is strongly tied to the ability to employ more efficient industrialprocesses. Modern compact heat exchangers can provide high compactness, a measureof the ratio of surface area-to-volume of a heat exchange. The microchannel heatexchanger studied here is a plate-type, robust heat exchanger that combines compact-ness, low pressure drop, high effectiveness, and the ability to operate with a very largepressure differential between hot and cold sides. The plates are etched and thereafterjoined by diffusion welding, resulting in extremely strong all-metal heat exchangercores. After bonding, any number of core blocks can be welded together to provide therequired flow capacity. This study explores the microchannel heat exchanger and drawsconclusions about diffusion welding/bonding for joining heat exchanger plates, with bothexperimental and computational modeling, along with existing challenges and gaps.Also, presented is a thermal design method for determining overall design specificationsfor a microchannel printed circuit heat exchanger for both supercritical (24MPa) andsubcritical (17MPa) Rankine power cycles. [DOI: 10.1115/1.4007578]Keywords: heat exchanger, diffusion welding, diffusion bonding, diffusion modeling,printed circuit heat exchanger, process application, thermodynamic modeling | |
01/01/2013 00:00:00 | |
Link to Article | |
7.1.4 | Microchannel heat exchanger |
Diffusion-Welded Microchannel Heat Exchanger for Industrial Processes | |
The goal of next generation reactors is to increase energy efficiency in the production of electricity and provide high-temperature heat for industrial processes. The efficient transfer of energy for industrial applications depends on the ability to incorporate effective heat exchangers between the nuclear heat transport system and the industrial process. The need for efficiency, compactness, and safety challenge the boundaries of existing heat exchanger technology. Various studies have been performed in attempts to update the secondary heat exchanger that is downstream of the primary heat exchanger, mostly because its performance is strongly tied to the ability to employ more efficient industrial processes. Modern compact heat exchangers can provide high compactness, a measure of the ratio of surface area-to-volume of a heat exchange. The microchannel heat exchanger studied here is a plate-type, robust heat exchanger that combines compactness, low pressure drop, high effectiveness, and the ability to operate with a very large pressure differential between hot and cold sides. The plates are etched and thereafter joined by diffusion welding, resulting in extremely strong all-metal heat exchanger cores. After bonding, any number of core blocks can be welded together to provide the required flow capacity. This study explores the microchannel heat exchanger and draws conclusions about diffusion welding/bonding for joining heat exchanger plates, with both experimental and computational modeling, along with existing challenges and gaps. Also, presented is a thermal design method for determining overall design specifications for a microchannel printed circuit heat exchanger for both supercritical (24 MPa) and subcritical (17 MPa) Rankine power cycles. | |
03/18/2013 00:00:00 | |
Link to Article | |
7.1.5 | Microchannel heat exchanger |
Heat transfer and pressure drop characteristics of a flat plate manifold microchannel heat exchanger in counter flow configuration | |
Abstract The design and performance testing of a single-phase, flat plate, manifold microchannel heat exchanger with water as the working fluid are discussed in this paper. The aim of this study was to explore the use of manifolding of microchannels for performance enhancement of plate heat exchangers for single-phase, low heat flux (process type) applications operating in a counter flow configuration. The paper discusses the design of the heat exchanger, followed by the experimental testing and numerical simulation results. The experimental tests reveal that the heat exchanger is capable of delivering an overall heat transfer coefficient of close to 20,000 W/m 2 K at flow rates as low as 20 g/s (corresponding to a microchannel Reynolds number of 30) and a pressure drop per length value of 5.85 bar/m. The experimental results also are compared with established counter flow heat exchanger e-NTU correlations to verify counter flow performance. Further, numerical simulation results for a single unit cell of the same geometry, which show reasonable agreement with the experimental results, are also described in this paper. The current work demonstrates successful use of microgrooves/microchannels for performance enhancement of plate heat exchangers for diverse industrial applications, including the refrigeration/air conditioning, process, and power production sectors. | |
03/01/2016 00:00:00 | |
Link to Article | |
7.1.6 | Microchannel heat exchanger |
Micro heat exchangers fabricated by diamond machining | |
Abstract Machining of thin metal foils with specially contoured diamond cutting tools allows the production of small and very smooth fluid microflow channels for micro heat exchanger applications. Heat exchanger plate wall thickness, as well as fin dimensions, may be carefully controlled and machined to dimensions on the order of tens of micrometers. The plates are stacked and bonded with the vacuum diffusion process to form a cross-flow, plate-type heat exchanger. These fabrication techniques allow the production of small heat exchangers with a very high volumetric heat transfer coefficient and inherent low weight. The design and fabrication process for a copper-based, cross-flow micro heat exchanger has been developed. The micro heat exchanger provided a volumetric heat transfer coefficient of nearly 45 MW/m 3 K under very conservative deisgn and operating conditions. This corresponds to a volumetric capacity nearly 20 times that of more conventional compact heat exchangers. High thermal capacity, coupled with low cost and ease of production, make these devices practical in areas where high thermal flux in a small volume is required. The methods and procedures for this type of micromachining closely parallel those for precision machining. | |
01/01/1994 00:00:00 | |
Link to Article | |
7.2 Hollow fiber heat exchanger
Hollow fiber heat exchangers are similar to shell and tube heat exchangers, however, they are much more compact and have large surface areas. Usually, they are formed using polymers. They can reduce the weight up to 50% compared to a traditional heat exchanger made out of metal.
Hollow fibers have an outer diameter 0.4-1.5 mm and can be produced by the extrusion process from a wide range of polymers such as PP (polypropylene), PC (polycarbonate), PA (polyamide), PEEK (poly-ether ether ketone), etc.
The wide range of materials results in an excellent chemical and corrosion-resistant heat exchanger. The heat exchanger is in some cases also environmental friendly as the fibers can be recycled.
**Research findings:**
\-Despite polymer materials’ low thermal conductivities (0.1–0.4 W/m K, which is 100–300 times lower than metals), by using hollow polymer fibers with the diameters less than 100 μm, the surface area/volume ratio of polymer hollow fiber heat exchangers can be very high. This makes them extremely efficient with superior thermal performance. Art. [#ARTNUM](#article-26752-2303822880)
3000 PP fibers weight 488 g and resulted in a 7.2 m² area of heat transfer. The highest heat transfers shown for liquid-gas are 450 W/m² K and 2100 W/m² K for liquid-liquid. Prototypes were able to handle a flow rate up to 700 L/hr with a heating duty of 6-13 kW.
Liquid-liquid, liquid-gas applications possible and liquid-steam. Most suitable for low-temperature temperature applications since the polymers are not resistant against high temperatures.
**Applications:**
* HVAC
* Food
* Chemical
* Biotech
* Building
* Automotive
* Electronics
* Energy storage
7.2.1 | Hollow fiber heat exchanger |
---|---|
Analysis of improved novel hollow fiber heat exchanger | |
Abstract Plastic heat exchangers have been of increasing interest for lower temperature applications because of their superior resistance to chemicals and fouling characteristics. However, the quite low thermal conductivity of polymer materials limits their widespread use and acceptance. The Polymeric Hollow Fiber Heat Exchangers (PHFHEs) with extremely large surface area overcome the constraint and have attracted more and more attention. In this study, we improve the heat transfer performance of the PHFHEs by optimizing their structure. The optimized way is to place the polypropylene net between the inlet and the outlet of the shell side. The hydrodynamics and heat transfer characteristics of the PHFHEs without net and with net were studied experimentally as well as numerically. The accuracy of the numerical model is demonstrated by the comparison with the experimental results. In this model, the heat transfer coefficient and the pressure drop, together with the velocity and temperature fields are obtained and presented to help analyzing the heat transfer characteristics of the PHFHEs without net and with net. It is found that at the same flow rate, the shell-side heat transfer coefficient per unit pressure drop of the PHFHEs with net is obviously higher than that without net, indicating the PHFHEs with net have their advantages over the ones without net. | |
06/01/2014 00:00:00 | |
Link to Article | |
7.2.2 | Hollow fiber heat exchanger |
Experimental and Theoretical Study on Heat and Mass Transfer of Hollow Fiber Membrane Heat Exchanger | |
An experiment on heat and mass transfer of a hollow fiber membrane heat exchanger proposed in our study was conducted with water as a working medium and Poly(vinylidene fluoride)(PDVF) as a membrane material.The influence of inlet temperature and flow rate of the solution on heat and mass transfer of the heat exchanger was explored under the counter flow condition.Moreover,a brass shell-and-tube heat exchanger with the same size as the membrane one was fabricated to compare its heat transfer,pressure drop and other character istics with those of the membrane heat exchanger.The experimental and theoretical studies indicate that although the thermal conductivity of the membrane materials is lower,the heat transfer capability of the membrane heat exchanger is higher due to its larger contact surface between the hot fluid and cold fluid,especially,the latent heat of the vapor caused by the mass transfer from the hot side to the cold side.The experimental result shows that the performance of the membrane heat exchanger is better than that of the metal one at the low flow rate under the experimental operation conditions.However,when the flow velocity in the tubes increases,the frictional resistance in the membrane heat exchanger is far larger than that in the metal heat exchanger.It seems that the present heat exchanger could be applied under low flow rate conditions. | |
01/01/2009 00:00:00 | |
Link to Article | |
7.2.3 | Hollow fiber heat exchanger |
Polymeric Hollow Fiber Heat Exchangers (PHFHEs): A New Type of Compact Heat Exchanger for Lower Temperature Applications | |
Plastic heat exchangers are characterized by an inferior thermal performance compared to their metal counterparts. Therefore, their usage is mainly limited to handling corrosive media or when ultra high purity is required, e.g., pharmaceutical industry. Polymeric Hollow Fiber Heat Exchangers (PHFHEs) have recently been proposed [1] as a new type of heat exchanger that can overcome these constraints and offer the same or better thermal performance than metallic shell and tube or plate heat exchangers while occupying a much smaller volume. In this paper we report our results for heat transfer in PHFHEs with both parallel and cross flow in the shell side of the device. Fibers made of polypropylene (PP) and polyetheretherketone (PEEK) were tested. In addition, steam condensation studies in PHFHEs are reported for the first time. The overall heat transfer coefficients achieved for water-water and water-brine systems are as high as 1400 Wm−2 K−1 . These values are higher than any value reported for plastic heat exchangers and comparable with commonly acceptable design values for metal shell and tube heat exchangers. Similar coefficients were obtained for steam condensation. Polymeric hollow fiber heat exchangers can also achieve high thermal effectiveness, large number of transfer units (NTU) and very small height of a transfer unit (HTU), if properly rated. If designed like commercial membrane contactors, they can achieve up to 12 transfer units in a single device, not longer than 60–70 cm! In addition, the conductance per unit volume PHFHEs achieved was up to one order of magnitude higher compared to metal heat transfer equipment. This superior thermal performance is also accompanied by considerably lower pressure drops. Therefore, the operation of PHFHEs will be characterized by a low operating cost. Combined with the much lower cost, lower weight and elimination of metal contamination polymer materials offer, it is obvious that PHFHEs constitute a potential substitute for metal heat exchangers on both thermal performance and economical grounds. Possible application fields include the food, pharmaceutical and biomedical industries as well as applications where corrosion resistant, light and very efficient devices are required, i.e., desalination, solar and offshore heat transfer applications.Copyright © 2005 by ASME | |
01/01/2005 00:00:00 | |
Link to Article | |
7.2.4 | Hollow fiber heat exchanger |
Polymeric Hollow Fiber Heat Exchangers: An Alternative for Lower Temperature Applications | |
Because of their better chemical resistance and fouling characteristics, plastic heat exchangers are of increasing interest for lower temperature applications. However, their lower thermal performance compared to that of metal heat exchangers has prevented their widespread use and acceptance. To overcome this constraint, polymeric hollow fiber heat exchangers (PHFHEs) are proposed as a new type of heat exchanger for lower temperature/pressure applications. In polypropylene-based PHFHEs, the overall heat-transfer coefficients achieved here, 647-1314 and 414-642 W m -2 K -1 for the water-water and ethanol-water systems, respectively, are comparable with accepted design values for metal shell-and-tube heat exchangers; further, for 20% of our water--water runs, it was higher than any value reported for plastic heat exchangers. The extremely large surface area/volume ratio of PHFHEs makes them more efficient than metal heat exchangers. Devices less than 30 cm (1 ft) long yielded efficiencies of up to 97.5%, up to 3.7 number of transfer units (NTU) and a height of a transfer unit (HTU) as low as 5 cm; the latter is 20 times less than the lower limit for shell-and-tube exchangers and 10 times less than the typical values for plate heat exchangers. PHFHEs achieve conductance/volume ratios 3-10 times higher than shell-and-tube devices accompanied by low-pressure drops, as low as 1 kPa/NTU, compared to 30 kPa/NTU for metal heat exchangers. Considering the much lower cost, weight, and elimination of metal contamination, PHFHEs can substitute metal heat exchangers on both thermal performance and economical grounds. | |
12/01/2004 00:00:00 | |
Link to Article | |
7.2.5 | Hollow fiber heat exchanger |
Recent research developments in polymer heat exchangers – A review | |
Due to their low cost, light weight and corrosive resistant features, polymer heat exchangers have been intensively studied by researchers with the aim to replace metallic heat exchangers in a wide range of applications. This paper reviews the development of polymer heat exchangers in the last decade, including cutting edge materials characteristics, heat transfer enhancement methods of polymer materials and a wide range of polymer heat exchanger applications. Theoretical modelling and experimental testing results have been reviewed and compared with literature. A recent development, the polymer micro-hollow fibre heat exchanger, is introduced and described. It is shown that polymer materials do hold promise for use in the construction of heat exchangers in many applications, but that a considerable amount of research is still required into material properties, thermal performance and life-time behaviour. | |
07/01/2016 00:00:00 | |
Link to Article | |
7.3 Meso heat exchanger
Meso heat exchangers have a very large surface area density >3000 m²/m³.
**Research findings:**
* The current investigation is concerned with the use of a heat exchanger that has a surface area density (β) of 4000 m2/m3. Art. [#ARTNUM](#article-26534-2792620623)
Still, in the development stage, meso heat exchanger can be applied in the most industry but are most suited for industries where compactness is extremely important.
7.3.1 | Meso heat exchanger |
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Transient response of a meso heat exchanger with temperature step variation | |
Abstract Heat exchangers are common components of many industrial, residential, and automotive systems. In automotive, heat exchangers are employed in engine cooling and air conditioning to transfer the undesired heat from the engine or the passenger compartment as a condenser, evaporator, inter-cooler, heater core, radiator, and oil cooler. Since, the thermal performance of heat exchangers influences the underhood automotive thermal management system, it is essential to characterize their dynamic response in general and specifically, when a sudden change to their operating parameters occur. Experimental measurements provide the scope for in depth understanding of the dynamic behavior of heat exchangers with respect to various parameters. This study investigates a liquid to gas cross flow meso heat exchanger subjected to transient conditions. Step variations in the hot fluid inlet temperature in the absence of mass flow rate disturbances was considered for 5 different levels ranging from 1.5 to 3.0, while other operating parameters are kept constant. The effect of step change on the thermal performance of a heat exchanger is demonstrated by both fluids outlet temperatures, heat transfer rate, effectiveness, and heat balance error. Results obtained show a faster response of the cold fluid outlet temperature compared to the hot fluid, however, an adverse effect is noticed for the heat transfer rate. Higher step changes in temperature lead to higher heat transfer rate, as expected; though, the hot side exhibited more heat transfer and higher effectiveness than the cold side. The hot fluid heat transfer rate and effectiveness display a non-linear increase reaching a peak, after which, it drops down at a slower rate compared to the cold fluid steady increase. A significant effect on normalized exit temperatures, heat transfer, and effectiveness at low step changes while it diminishes at higher step changes. The key element of this work is the use of meso heat exchanger to examine the transient conditions effect on its performance. This work covers a wide range of temperature step changes and aims to enrich the limited experimental database of dynamic response of heat exchangers. The outcome of this work is of interest to designers for thermal testing, characterization, and performance enhancement of compact heat exchangers. | |
07/01/2018 00:00:00 | |
Link to Article | |
7.4 Microjet heat exchanger
This paper describes the development of heat exchanger with microjet technology, proposed for a waste heat recovery from a range of processes. The article presents a comprehensive study on the heat transfer enhancement in a prototype heat exchanger. The heat exchanger is based on multiple jet impingement on the cylindrical heat transfer surface. It comprises four coaxial pipes (a supply channel and a return channel for two fluids). The design of the heat is based on availability on the market standardized materials. Art. [#ARTNUM](#article-26216-2571195246) Its essential core is a series of plates. Impinging jets are created by introducing plates with four nozzles of 400 and 600 µm in diameter. The nozzles were created by drilling 1 mm thick plate. These plates are separated by spacers/gaskets made of PTFE. Microjet geometry can be varied by exchanging the nozzle plates and spacers of the heat exchanger. Art. [#ARTNUM](#article-26216-2278329116)
This type of heat exchanger is still under development, studied applications are waste heat recovery, specifically in organic Rankine cycles.
7.4.1 | Microjet heat exchanger |
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Applicability of arrays of microjet heat transfer correlations to design compact heat exchangers | |
Abstract The article presents experimental studies on a compact heat exchanger with heat transfer intensification by means of impinging microjets. The pursuit to provide high performance of heat exchangers is a response to the demand both in economics and in the universal tendency to miniaturization of industrial equipment. This paper presents the design and tests of a prototype, microjet heat exchanger. The modular design of the heat exchanger allows to change its geometrical dimensions, as well as changing the heat exchange membrane material. The study of heat transfer in water–water flow allows to determine the heat transfer efficiency, the characteristics of heat transfer, and the heat transfer coefficient values. Data were collected for the pressure drops in heat exchanger not exceeding 15 kPa, i.e. such as in conventional heat exchangers. Hydraulic characteristics of a model heat exchanger were obtained. Experimental values of heat transfer for jet impingement were calculated by means of Wilson's plot method. Obtained values of heat transfer coefficient were compared with literature correlations. Authors also proposed their own empirical correlation for jet impingement heat transfer coefficient. | |
05/01/2016 00:00:00 | |
Link to Article | |
7.4.2 | Microjet heat exchanger |
Design and experimental investigations of a cylindrical microjet heat exchanger for waste heat recovery systems | |
Compact heat exchangers have more and more applications in many areas, including the HVAC, food and petrochemical industry. This paper describes the development of heat exchanger technology for waste heat recovery (WHR) from a range of processes. Case-study testing shows that the proposed heat exchanger can successfully enhance heat transfer and recover waste heat in a range of applications making them economically, environmentally and technically feasible. The heat exchanger is based on multiple jet impingement on the cylindrical heat transfer surface. It comprises four coaxial pipes (a supply channel and a return channel for two fluids). The design of the heat is based on available on the market standardized materials. The study of heat transfer in water-water flow allows determining the heat transfer efficiency and the heat transfer coefficient values. Data were collected for the pressure drops in heat exchanger not exceeding 15 kPa, i.e. such as in conventional heat exchangers. Hydraulic characteristics of a prototype heat exchanger were obtained. Experimental values of heat transfer for jet impingement were calculated. Obtained values of heat transfer coefficient were compared with literature correlations. A comparison of results of thermal-flow performance with double pipe heat exchanger indicated that the tested device in low flow rates obtains higher heat transfer coefficients, heat transfer increased 50%. The pressure losses of the novel heat exchanger are lower than standard double pipe heat exchanger. | |
03/01/2017 00:00:00 | |
Link to Article | |
7.5 Marbond heat exchanger
The Marbond heat exchanger/reactor family of products is the latest truly innovative design to enter the compact heat exchanger marketplace. Produced by Chart Marston at their UK factory, an ‘opened up' version of the Marbond unit is shown in the figure (scale — the unit shown is about the size of a lap-top computer with channels about 1 mm hydraulic diameter). It extends the choice of users who are looking for high integrity, highly compact units able to operate over a range of pressures and temperatures not met with more conventional gasketed or welded CHEs. The manufacturing procedures are similar to those of the PCHE (chemical etching and diffusion bonding), but the construction allows the use of small passageways, which significantly increases the porosity of the heat exchanger core. This can result, in appropriate applications, in a substantially higher area density than the PCHE. For example, a doubling of porosity, other factors being equal, results in a halving of the volume for a given surface area. The design is particularly versatile in terms of the number of passes and number of streams, and the type can be used for a wide variety of duties involving single-phase liquids and gases or two-phase streams, as well as for reactions. Art. [#ARTNUM](#article-26535-1989674565)
Patent
7.5.1 | Marbond heat exchanger |
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Compact heat exchangers, enhancement and heat pumps | |
Abstract In order to achieve widespread use of heat pumps across the full spectrum of potential applications, it is critical that the first cost of the units is acceptable. There are many factors influencing this cost, including the number of units manufactured, the ease of installation, the complexity of the control requirements, and the cost of the working fluid(s). A common feature of all heat pump cycles is the presence of at least one heat exchanger, indeed some heat-driven cycles are composed almost entirely of heat exchangers, each having a different but critical role to play. There are several important aspects of heat exchangers that can help to reduce first cost of these components and the system, (in addition to the possible positive impact on coefficient of performance). Two of these are discussed here — compact heat exchangers (CHEs) and heat transfer enhancement. The latter may be directly associated with CHEs but can be equally beneficial in reducing approach temperature differences in 'conventional' shell and tube heat exchangers. Both are essential features of many intensified processes, which the author argues need compatible heat pumps if the market for the latter is to flourish. In this paper, the most recent types of CHE are described, with emphasis on the benefits they can bring to heat pump first cost and performance. Heat transfer enhancement in heat pumps is also reviewed. | |
06/01/2002 00:00:00 | |
Link to Article | |
8. Trends
BackThere are some trends in heat exchangers that affect their design or material use.
8.1 3D printed heat exchangers
By 3D printing complex structures can be made, usually of the shell and tube type heat exchangers. Common shapes that are employed are Y-type and H-type tubes, as well as spirals, but the possibilities of 3D-printed heat exchangers are almost limitless. Especially for compact heat exchangers, they are interesting. Polymer heat exchangers can be 3D printed as well.
**Research findings:**
* In the present study, three-dimensional (3D) fractal-tree-like heat exchangers were designed and manufactured using 3D printing technology. Art. [#ARTNUM](#article-26220-2884496616)
3D printing of heat exchangers is under development, prototypes are under testing now.
Partner
8.1.1 | 3D printed heat exchangers |
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Cooling of Windings in Electric Machines via 3D Printed Heat Exchanger | |
This paper presents a novel use of 3D printed heat exchangers for advanced thermal management of electric machines. Thermal and computational fluid dynamics models are used to quantify the effectiveness of the 3D printed, Direct Winding Heat eXchangers (3D-DWHX). 3D printing enables complex flow geometries to be produced which facilitates the integration of the heat exchanger and reduces component count. The use of dielectric polymer for the heat exchanger allows direct contact with high voltage components to minimize the thermal resistance between windings and coolant. By occupying the otherwise unused space between double layer concentrated windings, there is no significant impact on the electromagnetic design. The result is an increased continuous power rating and power density of electric machines. | |
09/01/2018 00:00:00 | |
Link to Article | |
8.1.2 | 3D printed heat exchangers |
Development of an additive manufacturing-enabled compact manifold microchannel heat exchanger | |
Abstract This paper discusses the design and performance characterization of a compact tubular manifold microchannel heat exchanger. The purpose of this study was to explore the role of more precise flow distribution in the heat exchanger utilizing an additively manufactured manifold for single-phase flow under low to moderate heat flux conditions. The heat exchanger uses a commercially available enhanced tube having a fin structure on its outer surface and helical pattern of grooves (rifling structure) on the inner bore of the tube. A 3D printed manifold made of ABS plastic was used to properly distribute the flow on the shell-side of the heat exchanger. Water was used as the working fluid for both shell and tube-sides. Single-phase experimental tests showed an overall heat transfer coefficient of 22,000 W / ( m 2 K ) and shell-side heat transfer coefficient of 45,000 W / ( m 2 K ) for the shell-side and tube-side water flow rates of 82 g / s and 806 g / s , respectively. The shell-side heat transfer coefficient was found to be an order of magnitude higher than that found in typical shell and tube and plate-type heat exchangers. | |
01/01/2019 00:00:00 | |
Link to Article | |
8.1.3 | 3D printed heat exchangers |
Experimental and numerical investigation of fractal-tree-like heat exchanger manufactured by 3D printing | |
Abstract The manufacturing difficulties of complex fractal-tree-like heat exchangers have limited their industrial applications, although many evidences have shown that they have significant advantages in heat transfer. Nevertheless, the emerging 3D printing technology has brought great opportunity for the development of complex structured device. In the present study, three-dimensional (3D) fractal-tree-like heat exchangers were designed and manufactured using 3D printing technology. Their performance was evaluated from both thermal and hydrodynamic perspectives, the flow characteristics were investigated in detail. The results show that a fractal-tree-like heat exchanger can improve hydrodynamic performance, reduce pressure drops and has great heat transfer ability. In general, the fractal-tree-like heat exchanger has a comprehensive advantage over the traditional spiral-tube exchangers as it has a higher value of coefficient of performance (COP). Furthermore, the 3D printing provides a visual, efficient, and precise approach in the present research. | |
02/01/2019 00:00:00 | |
Link to Article | |
8.2 Nano fluids-based
In recent years, adding solid particles to a heat transfer medium has been one of the considerable techniques for increasing heat transfer rate in heat exchangers. Although they have drawn many attentions, they cause some problems such as high-pressure drop, abrasion, clogging and sedimentation. But using nanofluids causes a relatively higher increase in heat transfer in comparison to solid particles. In order to tackle above-mentioned problems, nanofluids are used with solid particles which are in very small sizes and low concentrations. Art. [#ARTNUM](#article-26217-2519485646)
Adding nanoparticles to heat exchange fluids improves their thermal conductivity and improves convection. Art. [#ARTNUM](#article-26217-2064293455)
Nanofluids are studied for their application in heat exchangers, they are commercially available.
8.2.1 | Nano fluids-based |
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A comprehensive review on double pipe heat exchangers | |
Abstract Growing need to develop and improve the effectiveness of heat exchangers has led to a broad range of investigations for increasing heat transfer rate along with decreasing the size and cost of the industrial apparatus accordingly. One of these many apparatus which are used in different industries is double pipe heat exchanger. This type of heat exchanger has drawn many attentions due to simplicity and wide range of usages. In recent years, several precise and invaluable studies have been performed in double pipe heat exchangers. In this review, the development procedure that this type of heat exchanger went through has been analyzed in details and the heat transfer enhancement methods in aforementioned heat exchangers have also been widely discussed. Having also tried the best to present a comprehensive research, the authors gathered information regarding the usage of these methods such as active, passive and compound methods which is worth noting that the studies concerning using passive methods in double pipe heat exchangers have been frequently cited. Moreover, various studies concerning using nanofluids in double pipe heat exchangers have been discussed in details. In this review, correlations of mostly Nusselt number and pressure drop coefficient are also presented. It is believed that this review provides new insights for further investigations. | |
01/01/2017 00:00:00 | |
Link to Article | |
8.2.2 | Nano fluids-based |
Analytical Investigation on Effect of Nanofluid Usage on Temperature Distribution in Double Pipe Heat Exchangers | |
Heat exchangers are used in many industrial areas for the purpose of meeting the heat transfer requirement. The widespread use of heat exchangers has led to a number of designs for increasing the heat transfer in the heat exchangers. One of the widely used heat exchanger types is the double pipe heat exchangers. In this study, the effects of nanofluid usage on temperature distribution in double pipe heat exchangers have been investigated analytically for laminar and steady-state flow conditions at a certain Reynolds number. Alumina based nanofluid with different particle sizes and water were used as heat transfer fluid in the inner and outer pipes and the fluid temperatures were compared with each other for all conditions. In addition that, for this conditions, the analytical results confirmed with the numerical results. | |
07/30/2017 00:00:00 | |
Link to Article | |
8.2.3 | Nano fluids-based |
Application of nanofluids in a shell-and-tube heat exchanger | |
Innovations in the field of nanotechnology have potential to improve industrial productivity and performance. One promising applications of this emerging technology is using nanofluids with enhanced thermal properties. Nanofluids, engineered colloidal suspensions consisting of nano-sized particles (less than 100nm) dispersed in a basefluid, have shown potential as industrial cooling fluids due to the enhanced heat transfer characteristics. Experiments are conducted to compare the overall heat transfer coefficient and pressure drop of water vs. nanofluids in a laboratory scale industrial type shell and tube heat exchanger. Three mass particle concentrations, 2%, 4% and 6%, of SiO2-water nanofluids are formulated by dispersing 20 nm diameter nano particles in desalinated water. Nanofluid and tap water are then circulated in the cold and hot loops, respectively, of the heat exchanger to avoid direct particle deposition on heater surfaces. Interestingly, experimental result show both augmentation and deterioration of heat transfer coefficient for nanofluids depending on the flow rate through the heat exchangers. This trend is consistent with an earlier reported observation for heat transfer in micro channels. This trend may be explained by the counter effect of the changes in thermo-physical properties of fluids together with the fouling on the heat exchanger surfaces. The measured pressure drop in the nanofluids flow shows an increase when compared to that of basefluid that could limit the use of nanofluids in heat exchangers for industrial application.Copyright © 2013 by ASME | |
06/16/2013 00:00:00 | |
Link to Article | |
8.2.4 | Nano fluids-based |
Application of nanofluids in plate heat exchanger: A review | |
Writing, or even making an attempt to write anything on or about Plate Heat Exchangers (Henceforth, PHE) would be no more than a futile effort to reassert and glorify an already stronghold state of PHEs, as is evident with the kind of multilayered and multi-tasked functions it performs, obviously in different forms, in various domains of work & walks of life, since a good long time. Nonetheless, in a bid to bring about a certain makeshift in the way the PHE has been functioning and sustaining, there was a need to revisit the structural pattern and the fluids that contribute to the performance of PHE. Summarily, this brings the researcher and designers to shift the focus not only from the conventional design but also to introduce a new substance which could further contribute to enhance the performance of the PHE. That is why, in recent times, the miniaturization of PHE and energy efficiency have become focal point of attention, discourse and research. While exploring for better alternates, the nanofluids have surfaced as probable (replaceable) substitutes. The Nanofluid is a relatively recent (in contrast with the PHEs) finding that promises, pronouncedly, greater heat absorbing and heat transport ability. The review article attempts to take a sneak peak into some of the important published articles that deal with the function and performance of PHEs using nanofluids. The first section of the paper presents observations by several authors on experimental and numerical results regarding thermal conductivity, viscosity, specific heat and heat transfer coefficients. The second section talks of application of nanofluids in plate heat exchangers. It has also examined the utility of nanofluids, particularly in PHEs, based on experiments and numerical studies. A review of previous works featuring experimental and numerical investigations seems to be suggesting, to the level of establishing, that nanofluids have great potential in increasing the overall performance of the plate heat exchangers. There is a further vital scope to work on the performance and utility of nanofluids and work on the equative proportions of its application, in the direction, the paper has made an attempt of. | |
11/01/2015 00:00:00 | |
Link to Article | |
8.2.5 | Nano fluids-based |
Recent advances in application of nanofluids in heat transfer devices: A critical review | |
Abstract This paper presents a critical review of heat transfer applications of nanofluids. The effects of nanoparticle concentration, size, shape, and nanofluid flow rate on Nusselt number, heat transfer coefficient, thermal conductivity, thermal resistance, friction factor and pressure drop from numerous studies reported recently are presented. Effects of various geometric parameters on heat transfer enhancement of system using nanofluids have also been reviewed. Heat transfer devices covered in this paper include radiators, circular tube heat exchangers, plate heat exchangers, shell and tube heat exchangers and heat sinks. Various correlations used for experimental validation or developed in reviewed studies are also compiled, compared and analyzed. The pros and cons associated to the applications of nanofluids in heat transfer devices are presented in details to determine the future direction of research in this arena. | |
04/01/2019 00:00:00 | |
Link to Article | |
8.2.6 | Nano fluids-based |
Water to Nanofluids Heat Transfer in Concentric Tube Heat Exchanger: Experimental Study | |
Abstract Concentric tube heat exchanger is a low cost, which increases reliability by restricting mixing of fluids exchanging heat. Concentric tube heat exchanger has potential application such as heat recovery from engine cooling circuit, oil cooling, desuperheating in refrigeration and air conditioning, dairy, and chemical industry, pharmaceutical industry, refinery, etc. This paper concentrate on an experimental study on concentric tube heat exchanger for water to nanofluids heat transfer with various concentrations of nanoparticles in to base fluids and application of nanofluids as working fluid. The experimental results on this type of heat exchanger configuration and water nanofluids could not be located in literature. Overall heat transfer coefficient was experimentally determined for a fixed heat transfer surface area with different volume fraction of nanoparticles in to base fluids and results were compared with pure water. It observed that, 3% nanofluids shown optimum performance with overall heat transfer coefficient 16% higher than water. | |
01/01/2013 00:00:00 | |
Link to Article | |
8.3 Polymer heat exchangers
The conventional heat exchanger manufactured in metal (such as stainless steel, copper and aluminium) has the disadvantages in terms of weight and cost. In addition, specially treated metal heat exchangers are needed if the working fluids are corrosive. Given these considerations, it is desirable to find an alternative material for heat exchangers that can overcome these disadvantages and also acquire comparable heat exchange efficiency and be easily fabricated. This is where the use of polymer heat exchanger comes into play. With the advantages of greater fouling and corrosion resistance, greater geometric flexibility and ease of manufacturing, reduced energy of formation and fabrication, and the ability to handle liquids and gases (i.e, single and two-phase duties), polymer heat exchangers have been widely studied and applied in the field of micro-electronic cooling devices, water desalination systems, solar water heating systems, liquid desiccant cooling systems, etc. Most importantly, the use of polymer materials offers substantial weight, space, and volume savings, which makes it more economically competitive compared with exchangers manufactured from many metallic alloys. Art. [#ARTNUM](#article-26457-2303822880)
Polymer heat exchangers exist in many forms, often used are shell and tube and plate configurations. Polymers are often used in compact heat exchangers. They are very suitable for corrosive liquid handling, especially were acid condensation is a problem. Flue gasses up to 350 °C can be handeled. Furthermore, they can be used to handle inorganic acids, brines and alkaline fluids in the metal finish, chemical and agricultural industries due their chemical resistance.
Multi-phase applications are possible.
**Applications:**
* HVAC
* Electronics/ computer
* Buildings
* Solar
* Seawater (desalination)
* Food
* Biotech / chemicals
* Automotive
Suppliers
8.3.1 | Polymer heat exchangers |
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Energy Efficient Polymers for Gas-Liquid Heat Exchangers | |
The compression process necessary for the liquefaction of natural gas on offshore platforms generates large amounts of heat, usually dissipated via sea water cooled plate heat exchangers. To date, the corrosive nature of sea water has mandated the use of metals, such as titanium, as heat exchanger materials, which are costly in terms of life cycle energy expenditure. This study investigates the potential of a commercially available, thermally conductive polymer material, filled with carbon fibers to enhance thermal conductivity by an order of magnitude or more. The thermofluid characteristics of a prototype polymer seawater-methane heat exchanger that could be used in the liquefaction of natural gas on offshore platforms are evaluated based on the total coefficient of performance (COP T ), which incorporates the energy required to manufacture a heat exchanger along with the pumping power expended over the lifetime of the heat exchanger, and compared with those of conventional heat exchangers made of metallic materials. The heat exchanger fabricated from a low energy, low thermal conductivity polymer is found to perform as well as, or better than, exchangers fabricated from conventional materials, over its full lifecycle. The analysis suggests that a COP T nearly double that of aluminum, and more than ten times that of titanium, could be achieved. Of the total lifetime energy use, 70% occurs in manufacturing for a thermally enhanced polymer heat exchanger compared with 97% and 85% for titanium and aluminum heat exchanges, respectively. The study demonstrates the potential of thermally enhanced polymer heat exchangers over conventional ones in terms of thermal performance and life cycle energy expenditure. | |
01/01/2010 00:00:00 | |
Link to Article | |
8.3.2 | Polymer heat exchangers |
Experimental characterization of heat transfer in an additively manufactured polymer heat exchanger | |
Abstract In addition to their low cost and weight, polymer heat exchangers offer good anticorrosion and antifouling properties. In this work, a cost effective air-water polymer heat exchanger made of thin polymer sheets using layer-by-layer line welding with a laser through an additive manufacturing process was fabricated and experimentally tested. The flow channels were made of 150 μm-thick high density polyethylene sheets, which were 15.5 cm wide and 29 cm long. The experimental results show that the overall heat transfer coefficient of 35–120 W/m 2 K is achievable for an air-water fluid combination for air-side flow rate of 3–24 L/s and water-side flow rate of 12.5 mL/s. In addition, by fabricating a very thin wall heat exchanger (150 μm), the wall thermal resistance, which usually becomes the limiting factor on polymer heat exchangers, was calculated to account for only 3% of the total thermal resistance. A comparison of the air-side heat transfer coefficient of the present polymer heat exchanger with some of the commercially available plain plate fin heat exchanger surfaces suggests that its performance in general is superior to that of common plain plate fin surfaces. | |
02/01/2017 00:00:00 | |
Link to Article | |
8.3.3 | Polymer heat exchangers |
Polymeric Hollow Fiber Heat Exchangers (PHFHEs): A New Type of Compact Heat Exchanger for Lower Temperature Applications | |
Plastic heat exchangers are characterized by an inferior thermal performance compared to their metal counterparts. Therefore, their usage is mainly limited to handling corrosive media or when ultra high purity is required, e.g., pharmaceutical industry. Polymeric Hollow Fiber Heat Exchangers (PHFHEs) have recently been proposed [1] as a new type of heat exchanger that can overcome these constraints and offer the same or better thermal performance than metallic shell and tube or plate heat exchangers while occupying a much smaller volume. In this paper we report our results for heat transfer in PHFHEs with both parallel and cross flow in the shell side of the device. Fibers made of polypropylene (PP) and polyetheretherketone (PEEK) were tested. In addition, steam condensation studies in PHFHEs are reported for the first time. The overall heat transfer coefficients achieved for water-water and water-brine systems are as high as 1400 Wm−2 K−1 . These values are higher than any value reported for plastic heat exchangers and comparable with commonly acceptable design values for metal shell and tube heat exchangers. Similar coefficients were obtained for steam condensation. Polymeric hollow fiber heat exchangers can also achieve high thermal effectiveness, large number of transfer units (NTU) and very small height of a transfer unit (HTU), if properly rated. If designed like commercial membrane contactors, they can achieve up to 12 transfer units in a single device, not longer than 60–70 cm! In addition, the conductance per unit volume PHFHEs achieved was up to one order of magnitude higher compared to metal heat transfer equipment. This superior thermal performance is also accompanied by considerably lower pressure drops. Therefore, the operation of PHFHEs will be characterized by a low operating cost. Combined with the much lower cost, lower weight and elimination of metal contamination polymer materials offer, it is obvious that PHFHEs constitute a potential substitute for metal heat exchangers on both thermal performance and economical grounds. Possible application fields include the food, pharmaceutical and biomedical industries as well as applications where corrosion resistant, light and very efficient devices are required, i.e., desalination, solar and offshore heat transfer applications.Copyright © 2005 by ASME | |
01/01/2005 00:00:00 | |
Link to Article | |
8.3.4 | Polymer heat exchangers |
Polymeric Hollow Fiber Heat Exchangers: An Alternative for Lower Temperature Applications | |
Because of their better chemical resistance and fouling characteristics, plastic heat exchangers are of increasing interest for lower temperature applications. However, their lower thermal performance compared to that of metal heat exchangers has prevented their widespread use and acceptance. To overcome this constraint, polymeric hollow fiber heat exchangers (PHFHEs) are proposed as a new type of heat exchanger for lower temperature/pressure applications. In polypropylene-based PHFHEs, the overall heat-transfer coefficients achieved here, 647-1314 and 414-642 W m -2 K -1 for the water-water and ethanol-water systems, respectively, are comparable with accepted design values for metal shell-and-tube heat exchangers; further, for 20% of our water--water runs, it was higher than any value reported for plastic heat exchangers. The extremely large surface area/volume ratio of PHFHEs makes them more efficient than metal heat exchangers. Devices less than 30 cm (1 ft) long yielded efficiencies of up to 97.5%, up to 3.7 number of transfer units (NTU) and a height of a transfer unit (HTU) as low as 5 cm; the latter is 20 times less than the lower limit for shell-and-tube exchangers and 10 times less than the typical values for plate heat exchangers. PHFHEs achieve conductance/volume ratios 3-10 times higher than shell-and-tube devices accompanied by low-pressure drops, as low as 1 kPa/NTU, compared to 30 kPa/NTU for metal heat exchangers. Considering the much lower cost, weight, and elimination of metal contamination, PHFHEs can substitute metal heat exchangers on both thermal performance and economical grounds. | |
12/01/2004 00:00:00 | |
Link to Article | |
8.3.5 | Polymer heat exchangers |
Recent research developments in polymer heat exchangers – A review | |
Due to their low cost, light weight and corrosive resistant features, polymer heat exchangers have been intensively studied by researchers with the aim to replace metallic heat exchangers in a wide range of applications. This paper reviews the development of polymer heat exchangers in the last decade, including cutting edge materials characteristics, heat transfer enhancement methods of polymer materials and a wide range of polymer heat exchanger applications. Theoretical modelling and experimental testing results have been reviewed and compared with literature. A recent development, the polymer micro-hollow fibre heat exchanger, is introduced and described. It is shown that polymer materials do hold promise for use in the construction of heat exchangers in many applications, but that a considerable amount of research is still required into material properties, thermal performance and life-time behaviour. | |
07/01/2016 00:00:00 | |
Link to Article | |
8.3.6 | Polymer heat exchangers |
Review of polymer compact heat exchangers, with special emphasis on a polymer film unit | |
This paper comprises of a general review on polymer compact heat exchangers (PCHEs). The first part outlines the types of polymers used and their respective characteristics. The second part presents the relative merits and the current PCHEs available in process industries. Following this, the recent advances in the field are addressed and finally, their future applications are discussed. In this paper, the types of polymers that can be used, as an alternative material of construction to metals in heat exchangers have been listed out. The relative merits of using polymers over metals are shown through a quantitative comparison, between PVDF and Hastelloy heat exchangers. When incorporating the same tube dimensions, thickness and fluid film coefficients, significant cost savings can be achieved using the PVDF exchanger. The descriptions of the three main categories of polymer compact heat exchangers currently available in industry are then provided to some detail. Following this, the polymer film compact heat exchanger (PFCHE) design is introduced to address the disadvantages of both metallic and present polymer heat exchangers. Notable design aspects of the unit are the use of thin (100 μm) polymer films to address the thermal conductivity deficiency and the adoption of laminar flows to deal with high-pressure drops. In addition, the presence of corrugations on the films promotes better fluid mixing, which increases the thermal performance of the unit. Due to its excellent thermal, chemical and mechanical stability, PEEK (poly ether ether ketone) is adopted in the PFCHE design. The benefits of the PFCHE design aspects (thin films, corrugations, narrow channels and developing laminar flow) are then highlighted. The paper concludes with a listing of the potential applications for the PFCHE in the process industries, based on the incentive provided by available polymer exchanger designs, particularly those incorporating thin polymer films. | |
11/01/2004 00:00:00 | |
Link to Article | |
8.4 Phase change material heat exchange
A phase change material (PCM) is a substance with a high heat of fusion which, melting and solidifying at a certain temperature, is capable of storing and releasing large amounts of energy. Heat is absorbed or released when the material changes from solid to liquid and vice versa; thus, PCMs are classified as latent heat storage (LHS) units. [\[Wiki\]](https://en.wikipedia.org/wiki/Phase-change_material)
Phase change materials are commonly studied for storage applications, however, they are also interesting for heat exchangers. Art. [#ARTNUM](#article-29666-953775078)
**Research findings:**
* The heat exchanger used in this work is a modular type which is similar to the shell and tube heat exchanger. The shell side is filled with Phase Change Materials (PCM) and airflow is through the tubes in the module. The modules of the heat exchanger are arranged one over other with air spacers in between each module. The air space provided between the module increases the retention time of the air for better heat transfer. Transient Computational Fluid Dynamics modelling is carried out for single air passage in a modular heat exchanger. It shows that the PCM phase transition time in the module in which different shape of fins is adopted. The module with rectangular fins has 17.2 % reduction in solidification compared with the plain module. Then the steady-state numerical analysis is accomplished to the whole module having the fin of high heat transfer so that pressure drop, flow and thermal characteristics across the module and the air spacers are determined for various air inlet velocities of 0.4 to 1.6 m/s. Art. [#ARTNUM](#article-29666-2075619204)
PCM can be applied in regenerative heat exchangers.
Suppliers
Projects
8.4.1 | Phase change material heat exchange |
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CFD modelling development and experimental validation of a phase change material (PCM) heat exchanger with spiral-wired tubes | |
Abstract Employing phase change materials (PCMs) for latent heat storage (LHS) application has a great potential to improve a solar thermal system performance. Despite this fact, the use of PCM in this area is quite limited due to the poor thermal conductivity of available PCMs. Therefore, heat transfer enhancement is one of the essential strategies that can overcome this obstacle. In this paper and related project, a PCM heat exchanger (HX) is purposely designed with spiral-wired tubes and integrated in an indirect solar assisted heat pump test system. Although the spiral-wired tube has not been applied in a PCM HX, it is expected to enhance significantly the PCM heat transfer and heat storage performance. To verify this and understand the PCM heat storage and releasement processes, a detailed 3D CFD model has been developed for the PCM HX and validated with measurements. The temperature variations and visualizations of the PCM during charging and discharging processes are therefore simulated and presented temporally. Furthermore, the effects of different inlet heat transfer fluid flow rates and temperatures on the PCM melting/solidification time are demonstrated in this study. Some significant simulation results have been obtained which can instruct efficiently the operation of the heat exchanger and its integration with the solar system. | |
02/01/2018 00:00:00 | |
Link to Article | |
8.4.2 | Phase change material heat exchange |
Extraction from large thermal storage systems using phase change materials and latent heat exchangers | |
An energy storage method and apparatus for extraction from large thermal storage systems using phase change materials and latent heat exchangers. This includes thermal heat extraction from, and charging of a large thermal storage tank containing thousands of megawatt hours of thermal energy, using the phase change of heat collection fluid and the phase change of molten phase change material for thermal storage use in generating electricity, steam, or for other industrial processes as implemented in the field of solar energy collection, thermal storage and extraction. The method and apparatus continuously removes thermal resistance that comes from the phase change material allowing operation at a high rate of efficiency. A heat exchanger is provided inside the storage tank thereby reducing heat losses, capital costs and space requirements compared to existing thermal storage systems. | |
12/20/2012 00:00:00 | |
Link to Article | |
8.4.3 | Phase change material heat exchange |
Phase change heat storage and release integrated heat exchanger | |
The invention provides a phase change heat storage and release integrated heat exchanger and belongs to the technical field of energy utilization. The phase change heat storage and release integrated heat exchanger is internally provided with two sets of coil pipes. The coil pipes A and the coil pipes B are arranged in a crossed mode. Each coil pipe is provided with two connectors. The connectors are formed in the upper portion of the phase change heat storage and release integrated heat exchanger. The side faces of the coil pipes have no openings. The coil pipes A are connected with a heat source medium. The coil pipes B are connected with a cold source medium. Each coil pipe is an S-shaped coil pipe formed by welding U-shaped elbows to straight pipes. The phase change heat storage and release integrated heat exchanger is internally provided with a metal frame used for supporting the coil pipes. Phase change materials are added into the phase change heat storage and release integrated heat exchanger and make direct contact with the coil pipes. Hot fluid transmits carried heat to cold fluid through the phase change materials. Through the design that heat storage pipes, heat release pipes and phase change heat storage and release media are separated, the functions of storing and releasing heat simultaneously are achieved; the heat storage amount of the device is more than three times that of water with the same volume; by means of the modular design, the phase change heat storage and release integrated heat exchanger is convenient to machine and suitable for industrial production. | |
11/11/2015 00:00:00 | |
Link to Article | |
8.4.4 | Phase change material heat exchange |
Study of heat transfer and pressure drop characteristics of air heat exchanger using PCM for free cooling applications | |
Free cooling is the process of storing the cool energy available in the night ambient air and using it during the day. The heat exchanger used in this work is a modular type which is similar to the shell and tube heat exchanger. The shell side is filled with Phase Change Materials (PCM) and air flow is through the tubes in the module. The modules of the heat exchanger are arranged one over other with air spacers in between each module. The air space provided in between the module in-creases the retention time of the air for better heat transfer. Transient Computational Fluid Dynamics modeling is carried out for single air passage in a modular heat exchanger. It shows that the PCM phase transition time in the module in which different shape of fins is adopted. The module with rectangular fins has 17.2 % reduction in solidification compared with the plain module. Then steady state numerical analysis is accomplished to the whole module having the fin of high heat transfer, so that pressure drop, flow and thermal characteristics across the module and the air spacers are deter-mined for various air inlet velocities of 0.4 to 1.6 m/s. To validate the computational results, experiments are carried out and the agreement was found to be good. | |
01/01/2016 00:00:00 | |
Link to Article | |
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