WO2021201944A2 - Heat exchanger with carbon nanotubes - Google Patents

Heat exchanger with carbon nanotubes Download PDF

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Publication number
WO2021201944A2
WO2021201944A2 PCT/US2021/012258 US2021012258W WO2021201944A2 WO 2021201944 A2 WO2021201944 A2 WO 2021201944A2 US 2021012258 W US2021012258 W US 2021012258W WO 2021201944 A2 WO2021201944 A2 WO 2021201944A2
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WO
WIPO (PCT)
Prior art keywords
heat exchanger
carbon nanotubes
plate
fluid
recited
Prior art date
Application number
PCT/US2021/012258
Other languages
French (fr)
Other versions
WO2021201944A3 (en
Inventor
Tianlei LI
Xiangxun LU
Original Assignee
Danfoss A/S
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Danfoss A/S filed Critical Danfoss A/S
Publication of WO2021201944A2 publication Critical patent/WO2021201944A2/en
Publication of WO2021201944A3 publication Critical patent/WO2021201944A3/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/18Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
    • F28F13/185Heat-exchange surfaces provided with microstructures or with porous coatings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2255/00Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes
    • F28F2255/20Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes with nanostructures

Definitions

  • HVAC heating, ventilation, and air conditioning
  • Refrigerant loops are known to include a compressor, a condenser, an expansion device, and an evaporator.
  • the compressor compresses the fluid, which then travels to a condenser, which in turn cools and condenses the fluid.
  • the refrigerant then goes to an expansion device, which decreases the pressure of the fluid, and to the evaporator, where the fluid is vaporized, completing a refrigeration cycle.
  • Heat exchangers are used to transfer heat between two or more fluids, and may be used in the condenser or evaporator, for example.
  • a plate heat exchanger includes, among other things, a plate having a metal surface, the plate is arranged in a flow of fluid.
  • a plurality of carbon nanotubes are arranged on the metal surface, and the carbon nanotubes are configured to exchange heat with the fluid.
  • the metal surface is curved.
  • each of the carbon nanotubes has at least one end bonded to the metal surface.
  • the plurality of carbon nanotubes have a variety of diameters, lengths and densities from a controlled manufacturing process.
  • the plurality of carbon nanotubes are deposited on the metal surface within a designated deposition area.
  • the plurality of carbon nanotubes have a varying density within the deposition area.
  • the carbon nanotubes have a first density on a first side of the deposition area, and a second density on a second side of the deposition area, the second density is lower than the first density.
  • a fluid inlet and a fluid outlet are arranged adjacent the first side of the deposition area.
  • the plurality of carbon nanotubes have a diameter between about 10 and 100 nanometers.
  • the plate is one of a plurality of plates arranged between a top plate and a back plate, the plurality of plates separating a plurality of chambers.
  • each of the plurality of plates has a plurality of carbon nanotubes.
  • the plate heat exchanger is used in a heating, ventilation, and air conditioning (HVAC) chiller system.
  • HVAC heating, ventilation, and air conditioning
  • a refrigerant system includes, among other things, a heat exchanger arranged along a fluid flow path, wherein the heat exchanger has a plate having a metal surface, and the plate is arranged in a flow of fluid.
  • a plurality of carbon nanotubes are arranged on the metal surface, and the carbon nanotubes are configured to exchange heat with the fluid.
  • the heat exchanger is arranged upstream of a compressor.
  • the heat exchanger is arranged downstream of a compressor.
  • the fluid is present in both a liquid and a vapor form in the heat exchanger.
  • each of the carbon nanotubes has at least one end bonded to the metal surface.
  • the plurality of carbon nanotubes have a variety of diameters, lengths and densities.
  • the plurality of carbon nanotubes have a diameter between about 10 and 100 nanometers.
  • Figure 1 schematically illustrates a refrigerant system.
  • Figure 2 schematically illustrates an example plate heat exchanger for use in a refrigerant system.
  • Figure 3 schematically illustrates an example plate for a plate heat exchanger.
  • Figure 4 schematically illustrates another example plate for a plate heat exchanger.
  • Figure 5 schematically illustrates an example carbon nanotube geometry for a plate heat exchanger.
  • Figure 6 illustrates example carbon nanotube geometries for a plate heat exchanger.
  • FIG. 1 illustrates a refrigerant system 10.
  • the refrigerant system 10 includes a main refrigerant loop, or circuit, 12 in communication with a compressor 14, a condenser 16, an evaporator 18, and an expansion device 20.
  • This refrigerant system 10 may be used in a chiller, for example.
  • a cooling tower may be in fluid communication with the condenser 16.
  • the main refrigerant loop 12 can include an economizer downstream of the condenser 16 and upstream of the expansion device 20.
  • FIG. 2 schematically illustrates an example plate heat exchanger 22.
  • the plate heat exchanger may be used in the condenser 16 or evaporator 18, for example.
  • the heat exchanger 22 is used to transfer heat between two or more fluids. In one example, the heat exchanger 22 transfers heat between refrigerant and water or refrigerant and air, for example.
  • the heat exchanger 22 has a plurality of plates 28 separating a plurality of chambers 24.
  • the plates 28 may be metallic. In a further embodiment, the plates 28 may be a thin corrugated metal, for example.
  • a first fluid 26 and a second fluid 30 flow through the plates 28 and chambers 24. The fluids 26, 30 pass through the plates 28 and chambers 24 via connecting pipes 32, 34, 36, 38.
  • the pipe 32 provides an inlet for the fluid 30, while pipe 34 provides a return flow path.
  • the pipe 36 provides an inlet for the fluid 26, while pipe 38 provides a return flow path.
  • the fluid 30 is a cold fluid
  • the fluid 26 is a hot fluid.
  • the fluids 26, 30 flow through the pipes 32, 34, 36, 38 and through alternating chambers 24.
  • the hot fluid 26 flows through chambers 24A while the cold fluid 30 flows through chambers 24B. Heat transfers from the hot fluid 26 to the cold fluid 30 through the plates 28 as the fluids 26, 30 flow through alternating chambers 24A, 24B, respectively.
  • the plates 28 may be arranged between a top plate 40 and a back plate 42. In some examples, a sensor 44 is arranged at the back plate 42.
  • FIG. 3 schematically illustrates an example plate 28 for a plate heat exchanger 22.
  • the plate 28 has a portion 50 between the pipes 32, 34, 36, 38.
  • the portion 50 corresponds to a heat exchanger zone, in which heat is transferred between the fluids 26, 30 and the plate 28.
  • the portion 50 of the plate 28 may be flat or curved, for example.
  • a plurality of carbon nanotubes are arranged on the portion 50.
  • the portion 50 covers the entire area of the plate 28, while in other examples, the portion 50 is small relative to the area of the plate 28. In one example, the portion 50 covers at least half of the area of the plate 28.
  • one or more plate 28 in the heat exchanger 28 has a carbon nanotube portion 50, while in other examples, all of the plates 28 have a carbon nanotube portion 50.
  • the carbon nanotubes increase the area of the heat exchange surface of the plates 28, which improves efficiency. The carbon nanotubes are shown and described more fully herein.
  • FIG 4 schematically illustrates another example plate 128 for a plate heat exchanger 22.
  • the plate 128 corresponds to the plate 28 of Figure 3, with like parts having reference numerals preappended with a “1.”
  • a density of carbon nanotubes varies across the portion 150.
  • fluid 130 flows between the pipes 132 and 134 across the portion 150 of the plate 128.
  • the carbon nanotubes are arranged more densely on a first side 152 of the portion 150 than on a second side 154.
  • a more dense carbon nanotube area provides a larger heat exchange area than a less dense carbon nanotube area.
  • the density of carbon nanotubes may be a gradient across some or all of the portion 150.
  • the density is varied over the portion 150 to optimize the fluid flow 130 across the plate 150.
  • the density may be tunable based on heat exchanger requirements at different locations.
  • the carbon nanotubes 160 are arranged on only part of the portion 150.
  • the carbon nanotube arrangement may vary across different plates 128 within the heat exchanger 22, in some examples.
  • FIG. 5 schematically illustrates an example carbon nanotube geometry for a plate heat exchanger 22.
  • a plurality of carbon nanotubes 60 extend from the portion 50 of the plate 28.
  • the carbon nanotubes 60 each have one end 62 that is bonded or constrained to the portion 50 of the plate 28.
  • the nanotubes 60 may be synthesized directly on the plate 28, or may be bonded to the surface of the plate 28.
  • Each of the carbon nanotubes 60 has a diameter D and length L.
  • the carbon nanotubes 60 may have differing lengths and diameters across the portion 50.
  • the length L and diameter D of the nanotubes 60 may be varied. For example, the length L may be longer for areas where there is a larger space between adjacent plates 28.
  • Figure 6 illustrates example carbon nanotube geometries for a plate heat exchanger 22.
  • This example shows several different nanotube diameters D.
  • the diameters of the nanotubes may be between about 10 and 100 nm, for example.
  • One example diameter Di is about 18.7 nanometers.
  • Another example diameter D2 is about 26.8 nm.
  • Another example diameter D3 is about 44.6 nm, and a fourth example diameter D4 is about 87.7 nm.
  • Different nanotubes 60 may have different diameters on the same plate 28. In other embodiments, all of the nanotubes 60 on the plate 28 may have the same diameter.
  • the size of the nanotubes 60 can change the heat exchange area, and thus alter the efficiency of the heat exchanger 22.
  • the nanotubes 60 are multiwalled carbon nanotubes.
  • the carbon nanotubes may have a variety of diameters, lengths and densities from a controlled manufacturing process.
  • the disclosed plate heat exchanger 22 may improve heat exchange efficiency by increasing the effective heat transfer area and optimizing the flow pattern in the chambers 24.
  • the carbon nanotubes 60 act as fins on the heat exchanger plates 28, increasing the heat exchange area between the plate 28 and the fluid 26, 30.
  • the carbon nanotubes 60 may reduce the drag between the solid plate 28 and the fluids 26, 30, which may reduce the pressure drop across the heat exchanger 22.
  • two phase flow is present, and at least one of the fluids 26, 30 is present in a liquid and vapor form.
  • the carbon nanotubes 60 may increase turbulent flow to avoid vapor and liquid separation, which may improve heat transfer distribution.
  • the position, density, and size of the carbon nanotubes 60 may allow for optimization of flow distribution of the fluids 26, 30 across the plates 28.
  • the CNTs 60 form a hydrophobic layer on the heat exchanger solid surface.
  • the formed liquid cannot stay on the heat exchanger surface and will be pushed away by the pressure. This may prevent a liquid thermal barrier forming between the heat exchanger solid surface and the gas and ensures the heat exchanger solid surface always exchanges energy was the gas directly. Such an arrangement may improve condenser efficiency.

Abstract

A plate heat exchanger according to an exemplary aspect of the present disclosure includes, among other things, a plate having a metal surface. The plate is arranged in a flow of fluid. A plurality of carbon nanotubes are arranged on the metal surface, and the carbon nanotubes are configured to exchange heat with the fluid.

Description

HEAT EXCHANGER WITH CARBON NANOTUBES
PRIORITY CLAIM
[0001] This application claims the benefit of United States Provisional Application No. 62/958,385, filed on January 8, 2020.
TECHNICAL FIELD
[0002] This disclosure relates to a heat exchanger device. The heat exchanger may be used in a heating, ventilation, and air conditioning (HVAC) chiller system, for example.
BACKGROUND
[0003] Refrigerant loops are known to include a compressor, a condenser, an expansion device, and an evaporator. The compressor compresses the fluid, which then travels to a condenser, which in turn cools and condenses the fluid. The refrigerant then goes to an expansion device, which decreases the pressure of the fluid, and to the evaporator, where the fluid is vaporized, completing a refrigeration cycle. Heat exchangers are used to transfer heat between two or more fluids, and may be used in the condenser or evaporator, for example.
SUMMARY
[0004] A plate heat exchanger according to an exemplary aspect of the present disclosure includes, among other things, a plate having a metal surface, the plate is arranged in a flow of fluid. A plurality of carbon nanotubes are arranged on the metal surface, and the carbon nanotubes are configured to exchange heat with the fluid.
[0005] In a further embodiment, the metal surface is curved.
[0006] In a further embodiment, the metal surface is flat. [0007] In a further embodiment, each of the carbon nanotubes has at least one end bonded to the metal surface.
[0008] In a further embodiment, the plurality of carbon nanotubes have a variety of diameters, lengths and densities from a controlled manufacturing process.
[0009] In a further embodiment, the plurality of carbon nanotubes are deposited on the metal surface within a designated deposition area.
[0010] In a further embodiment, the plurality of carbon nanotubes have a varying density within the deposition area.
[0011] In a further embodiment, the carbon nanotubes have a first density on a first side of the deposition area, and a second density on a second side of the deposition area, the second density is lower than the first density.
[0012] In a further embodiment, a fluid inlet and a fluid outlet are arranged adjacent the first side of the deposition area.
[0013] In a further embodiment, the plurality of carbon nanotubes have a diameter between about 10 and 100 nanometers.
[0014] In a further embodiment, the plate is one of a plurality of plates arranged between a top plate and a back plate, the plurality of plates separating a plurality of chambers.
[0015] In a further embodiment, each of the plurality of plates has a plurality of carbon nanotubes.
[0016] In a further embodiment, the plate heat exchanger is used in a heating, ventilation, and air conditioning (HVAC) chiller system.
[0017] A refrigerant system according to an exemplary aspect of the present disclosure includes, among other things, a heat exchanger arranged along a fluid flow path, wherein the heat exchanger has a plate having a metal surface, and the plate is arranged in a flow of fluid. A plurality of carbon nanotubes are arranged on the metal surface, and the carbon nanotubes are configured to exchange heat with the fluid.
[0018] In a further embodiment, the heat exchanger is arranged upstream of a compressor.
[0019] In a further embodiment, the heat exchanger is arranged downstream of a compressor.
[0020] In a further embodiment, the fluid is present in both a liquid and a vapor form in the heat exchanger.
[0021] In a further embodiment, each of the carbon nanotubes has at least one end bonded to the metal surface.
[0022] In a further embodiment, the plurality of carbon nanotubes have a variety of diameters, lengths and densities.
[0023] In a further embodiment, the plurality of carbon nanotubes have a diameter between about 10 and 100 nanometers.
BRIEF DESCRIPTION OF THE DRAWINGS
[0024] Figure 1 schematically illustrates a refrigerant system.
[0025] Figure 2 schematically illustrates an example plate heat exchanger for use in a refrigerant system.
[0026] Figure 3 schematically illustrates an example plate for a plate heat exchanger.
[0027] Figure 4 schematically illustrates another example plate for a plate heat exchanger.
[0028] Figure 5 schematically illustrates an example carbon nanotube geometry for a plate heat exchanger. [0029] Figure 6 illustrates example carbon nanotube geometries for a plate heat exchanger.
DETAILED DESCRIPTION
[0030] Figure 1 illustrates a refrigerant system 10. The refrigerant system 10 includes a main refrigerant loop, or circuit, 12 in communication with a compressor 14, a condenser 16, an evaporator 18, and an expansion device 20. This refrigerant system 10 may be used in a chiller, for example. In that example, a cooling tower may be in fluid communication with the condenser 16. While a particular example of the refrigerant system 10 is shown, this application extends to other refrigerant system configurations, including configurations that do not include a chiller. For instance, the main refrigerant loop 12 can include an economizer downstream of the condenser 16 and upstream of the expansion device 20.
[0031] Figure 2 schematically illustrates an example plate heat exchanger 22. The plate heat exchanger may be used in the condenser 16 or evaporator 18, for example. The heat exchanger 22 is used to transfer heat between two or more fluids. In one example, the heat exchanger 22 transfers heat between refrigerant and water or refrigerant and air, for example. The heat exchanger 22 has a plurality of plates 28 separating a plurality of chambers 24. The plates 28 may be metallic. In a further embodiment, the plates 28 may be a thin corrugated metal, for example. A first fluid 26 and a second fluid 30 flow through the plates 28 and chambers 24. The fluids 26, 30 pass through the plates 28 and chambers 24 via connecting pipes 32, 34, 36, 38. In the illustrated example, the pipe 32 provides an inlet for the fluid 30, while pipe 34 provides a return flow path. The pipe 36 provides an inlet for the fluid 26, while pipe 38 provides a return flow path. [0032] In the illustrated example, the fluid 30 is a cold fluid, and the fluid 26 is a hot fluid. The fluids 26, 30 flow through the pipes 32, 34, 36, 38 and through alternating chambers 24. For example, the hot fluid 26 flows through chambers 24A while the cold fluid 30 flows through chambers 24B. Heat transfers from the hot fluid 26 to the cold fluid 30 through the plates 28 as the fluids 26, 30 flow through alternating chambers 24A, 24B, respectively. The plates 28 may be arranged between a top plate 40 and a back plate 42. In some examples, a sensor 44 is arranged at the back plate 42.
[0033] Figure 3 schematically illustrates an example plate 28 for a plate heat exchanger 22. The plate 28 has a portion 50 between the pipes 32, 34, 36, 38. The portion 50 corresponds to a heat exchanger zone, in which heat is transferred between the fluids 26, 30 and the plate 28. The portion 50 of the plate 28 may be flat or curved, for example. A plurality of carbon nanotubes are arranged on the portion 50. In some examples, the portion 50 covers the entire area of the plate 28, while in other examples, the portion 50 is small relative to the area of the plate 28. In one example, the portion 50 covers at least half of the area of the plate 28. In some examples, one or more plate 28 in the heat exchanger 28 has a carbon nanotube portion 50, while in other examples, all of the plates 28 have a carbon nanotube portion 50. The carbon nanotubes increase the area of the heat exchange surface of the plates 28, which improves efficiency. The carbon nanotubes are shown and described more fully herein.
[0034] Figure 4 schematically illustrates another example plate 128 for a plate heat exchanger 22. To the extent not otherwise described or shown, the plate 128 corresponds to the plate 28 of Figure 3, with like parts having reference numerals preappended with a “1.” In this example, a density of carbon nanotubes varies across the portion 150. In the illustrated view, fluid 130 flows between the pipes 132 and 134 across the portion 150 of the plate 128. The carbon nanotubes are arranged more densely on a first side 152 of the portion 150 than on a second side 154. A more dense carbon nanotube area provides a larger heat exchange area than a less dense carbon nanotube area. Although the figure shows two densities at sides 152, 154, the density of carbon nanotubes may be a gradient across some or all of the portion 150. In this example, the density is varied over the portion 150 to optimize the fluid flow 130 across the plate 150. The density may be tunable based on heat exchanger requirements at different locations. In some examples, the carbon nanotubes 160 are arranged on only part of the portion 150. The carbon nanotube arrangement may vary across different plates 128 within the heat exchanger 22, in some examples.
[0035] Figure 5 schematically illustrates an example carbon nanotube geometry for a plate heat exchanger 22. A plurality of carbon nanotubes 60 extend from the portion 50 of the plate 28. The carbon nanotubes 60 each have one end 62 that is bonded or constrained to the portion 50 of the plate 28. The nanotubes 60 may be synthesized directly on the plate 28, or may be bonded to the surface of the plate 28. Each of the carbon nanotubes 60 has a diameter D and length L. The carbon nanotubes 60 may have differing lengths and diameters across the portion 50. The length L and diameter D of the nanotubes 60 may be varied. For example, the length L may be longer for areas where there is a larger space between adjacent plates 28.
[0036] Figure 6 illustrates example carbon nanotube geometries for a plate heat exchanger 22. This example shows several different nanotube diameters D. The diameters of the nanotubes may be between about 10 and 100 nm, for example. One example diameter Di is about 18.7 nanometers. Another example diameter D2 is about 26.8 nm. Another example diameter D3 is about 44.6 nm, and a fourth example diameter D4 is about 87.7 nm. Different nanotubes 60 may have different diameters on the same plate 28. In other embodiments, all of the nanotubes 60 on the plate 28 may have the same diameter. The size of the nanotubes 60 can change the heat exchange area, and thus alter the efficiency of the heat exchanger 22. In some examples, the nanotubes 60 are multiwalled carbon nanotubes. The carbon nanotubes may have a variety of diameters, lengths and densities from a controlled manufacturing process. [0037] The disclosed plate heat exchanger 22 may improve heat exchange efficiency by increasing the effective heat transfer area and optimizing the flow pattern in the chambers 24. The carbon nanotubes 60 act as fins on the heat exchanger plates 28, increasing the heat exchange area between the plate 28 and the fluid 26, 30. The carbon nanotubes 60 may reduce the drag between the solid plate 28 and the fluids 26, 30, which may reduce the pressure drop across the heat exchanger 22. In some heat exchangers 22, two phase flow is present, and at least one of the fluids 26, 30 is present in a liquid and vapor form. In these examples, the carbon nanotubes 60 may increase turbulent flow to avoid vapor and liquid separation, which may improve heat transfer distribution. The position, density, and size of the carbon nanotubes 60 may allow for optimization of flow distribution of the fluids 26, 30 across the plates 28.
[0038] For a condenser application, the CNTs 60 form a hydrophobic layer on the heat exchanger solid surface. When the gas condenses within the heat exchanger, the formed liquid cannot stay on the heat exchanger surface and will be pushed away by the pressure. This may prevent a liquid thermal barrier forming between the heat exchanger solid surface and the gas and ensures the heat exchanger solid surface always exchanges energy was the gas directly. Such an arrangement may improve condenser efficiency.
[0039] Terms such “generally,” “about,” and “substantially” are not intended to be boundary less terms, and should be interpreted consistent with the way one skilled in the art would interpret those terms.
[0040] Although the different examples have the specific components shown in the illustrations, embodiments of this disclosure are not limited to those particular combinations. It is possible to use some of the components or features from one of the examples in combination with features or components from another one of the examples.
[0041] One of ordinary skill in this art would understand that the above-described embodiments are exemplary and non-limiting. That is, modifications of this disclosure would come within the scope of the claims. Accordingly, the following claims should be studied to determine their true scope and content.

Claims

1. A plate heat exchanger, comprising: a plate having a metal surface, the plate arranged in a flow of fluid; and a plurality of carbon nanotubes arranged on the metal surface, the carbon nanotubes are configured to exchange heat with the fluid.
2. The plate heat exchanger as recited in claim 1, wherein the metal surface is curved.
3. The plate heat exchanger as recited in claim 1, wherein the metal surface is flat.
4. The plate heat exchanger as recited in claim 1, wherein each of the carbon nanotubes has at least one end bonded to the metal surface.
5. The plate heat exchanger as recited in claim 1, wherein the plurality of carbon nanotubes have a variety of diameters, lengths and densities from a controlled manufacturing process.
6. The plate heat exchanger as recited in claim 1, wherein the plurality of carbon nanotubes are deposited on the metal surface within a designated deposition area.
7. The plate heat exchanger as recited in claim 6, wherein the plurality of carbon nanotubes have a varying density within the deposition area.
8. The plate heat exchanger as recited in claim 7, wherein the carbon nanotubes have a first density on a first side of the deposition area, and a second density on a second side of the deposition area, the second density is lower than the first density.
9. The plate heat exchanger as recited in claim 8, wherein a fluid inlet and a fluid outlet are arranged adjacent the first side of the deposition area.
10. The plate heat exchanger as recited in claim 1, wherein the plurality of carbon nanotubes have a diameter between about 10 and 100 nanometers.
11. The plate heat exchanger as recited in claim 1 , wherein the plate is one of a plurality of plates arranged between a top plate and a back plate, the plurality of plates separating a plurality of chambers.
12. The plate heat exchanger as recited in claim 11, wherein each of the plurality of plates has a plurality of carbon nanotubes.
13. The plate heat exchanger as recited in claim 1, wherein the plate heat exchanger is used in a heating, ventilation, and air conditioning (HVAC) chiller system.
14. A refrigerant system, comprising: a heat exchanger arranged along a fluid flow path, wherein the heat exchanger has a plate having a metal surface, the plate is arranged in a flow of fluid, and a plurality of carbon nanotubes are arranged on the metal surface, the carbon nanotubes are configured to exchange heat with the fluid.
15. The refrigerant system of claim 14, wherein the heat exchanger is arranged upstream of a compressor.
16. The refrigerant system of claim 14, wherein the heat exchanger is arranged downstream of a compressor.
17. The refrigerant system of claim 14, wherein the fluid is present in both a liquid and a vapor form in the heat exchanger.
18. The refrigerant system of claim 14, wherein each of the carbon nanotubes has at least one end bonded to the metal surface.
19. The refrigerant system of claim 14, wherein the plurality of carbon nanotubes have a variety of diameters, lengths and densities.
20. The refrigerant system of claim 14, wherein the plurality of carbon nanotubes have a diameter between about 10 and 100 nanometers.
PCT/US2021/012258 2020-01-08 2021-01-06 Heat exchanger with carbon nanotubes WO2021201944A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US202062958385P 2020-01-08 2020-01-08
US62/958,385 2020-01-08

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Publication number Priority date Publication date Assignee Title
US9896341B2 (en) * 2012-04-23 2018-02-20 Seerstone Llc Methods of forming carbon nanotubes having a bimodal size distribution
JP6118540B2 (en) * 2012-11-08 2017-04-19 新光電気工業株式会社 Heat dissipation component and manufacturing method thereof
JP6405914B2 (en) * 2014-11-11 2018-10-17 株式会社デンソー HEAT EXCHANGE DEVICE AND HEAT EXCHANGE DEVICE MANUFACTURING METHOD
EP3136434A1 (en) * 2015-08-26 2017-03-01 ETH Zurich Thermal interface element
US20190107343A1 (en) * 2017-10-09 2019-04-11 Hamilton Sundstrand Corporation Functionally graded composite polymer for heat exchanger

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