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WO2006101563A2 - Multi-part heat exchanger - Google Patents

Multi-part heat exchanger Download PDF

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Publication number
WO2006101563A2
WO2006101563A2 PCT/US2005/047524 US2005047524W WO2006101563A2 WO 2006101563 A2 WO2006101563 A2 WO 2006101563A2 US 2005047524 W US2005047524 W US 2005047524W WO 2006101563 A2 WO2006101563 A2 WO 2006101563A2
Authority
WO
WIPO (PCT)
Prior art keywords
heat exchanger
flow path
refrigerant
flow
components
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/US2005/047524
Other languages
French (fr)
Other versions
WO2006101563A3 (en
Inventor
Tobias Sienel
Yu Chen
Parmesh Verma
Hans-Joachim Huff
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Taylor Commercial FoodService LLC
Original Assignee
Carrier Comercial Refrigeration Inc
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 Carrier Comercial Refrigeration Inc filed Critical Carrier Comercial Refrigeration Inc
Priority to HK08111972.1A priority Critical patent/HK1120103B/en
Priority to US11/908,418 priority patent/US20080184731A1/en
Priority to JP2008501863A priority patent/JP4705157B2/en
Priority to ES05856004.6T priority patent/ES2580080T3/en
Priority to EP05856004.6A priority patent/EP1872068B1/en
Publication of WO2006101563A2 publication Critical patent/WO2006101563A2/en
Anticipated expiration legal-status Critical
Publication of WO2006101563A3 publication Critical patent/WO2006101563A3/en
Ceased legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B6/00Compression machines, plants or systems, with several condenser circuits
    • F25B6/04Compression machines, plants or systems, with several condenser circuits arranged in series
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/008Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D19/00Arrangement or mounting of refrigeration units with respect to devices or objects to be refrigerated, e.g. infrared detectors
    • F25D19/02Arrangement or mounting of refrigeration units with respect to devices or objects to be refrigerated, e.g. infrared detectors plug-in type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/06Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
    • F25B2309/061Compression machines, plants or systems characterised by the refrigerant being carbon dioxide with cycle highest pressure above the supercritical pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D23/00General constructional features
    • F25D23/003General constructional features for cooling refrigerating machinery
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D2317/00Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass
    • F25D2317/06Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass with forced air circulation
    • F25D2317/065Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass with forced air circulation characterised by the air return
    • F25D2317/0651Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass with forced air circulation characterised by the air return through the bottom
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D2317/00Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass
    • F25D2317/06Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass with forced air circulation
    • F25D2317/066Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass with forced air circulation characterised by the air supply
    • F25D2317/0661Details or arrangements for circulating cooling fluids; Details or arrangements for circulating gas, e.g. air, within refrigerated spaces, not provided for in other groups of this subclass with forced air circulation characterised by the air supply from the bottom
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D2323/00General constructional features not provided for in other groups of this subclass
    • F25D2323/002Details for cooling refrigerating machinery
    • F25D2323/0026Details for cooling refrigerating machinery characterised by the incoming air flow
    • F25D2323/00264Details for cooling refrigerating machinery characterised by the incoming air flow through the front bottom part
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D2323/00General constructional features not provided for in other groups of this subclass
    • F25D2323/002Details for cooling refrigerating machinery
    • F25D2323/0027Details for cooling refrigerating machinery characterised by the out-flowing air
    • F25D2323/00271Details for cooling refrigerating machinery characterised by the out-flowing air from the back bottom
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D2500/00Problems to be solved
    • F25D2500/02Geometry problems

Definitions

  • the invention relates to vapor compression systems and, more particularly, to a heat exchanger configuration for such a system.
  • a refrigeration system which includes a compressor for driving a refrigerant along a flow path in at least a first mode of system operation; a first heat exchanger along the flow path downstream of the compressor in the first mode; a second heat exchanger along the flow path upstream of the compressor in the first mode; and an expansion device in the flow path downstream of the first heat exchanger and upstream of the second heat exchanger in the first mode, wherein the first heat exchanger comprises a plurality of heat exchanger components arranged along a flow path of heat exchange fluid for the first heat exchanger.
  • the heat exchanger components can be positioned in smaller available areas within the unit and thereby use space more efficiently.
  • flow to these heat exchange components can be routed so as to provide counter flow of the heat exchange fluid, for example air, with the refrigerant.
  • the system of the present invention can be at least partially if not entirely incorporated into a cassette which can be readily interchanged within the existing housing or case of a refrigerator unit to allow replacement of the cassette when needed without replacing the entire unit.
  • FIG. 1 is a perspective view of a system having a multi-part heat exchanger according to the invention.
  • FIG. 2 is a schematic illustration of a multi-part heat exchanger system according to the invention.
  • FIG.3 illustrates the refrigerant and air flow in a system according to the invention.
  • the invention relates to a vapor compression system of a refrigerator unit and, more particularly, to the arrangement of a heat exchanger in a vapor compression system, preferably in a transcritical vapor compression system.
  • heat exchange medium such as air
  • greater contact area between the heat exchanger and heat exchange medium is obtained by utilizing all potentially available spaces within a particular vapor compression system to house additional components of a heat exchanger, such that the heat exchanger is implemented in a series or plurality of heat exchange components. In this manner, small available spaces are nevertheless utilized to increase heat exchange efficiency and, therefore, efficiency of the overall system.
  • FIG. 1 shows a system in accordance with the present invention.
  • system 10 which, in this particular embodiment, is the vapor compression system for a bottle cooler refrigeration assembly.
  • FIG. 1 shows the lower portion of such an assembly, including a housing 12 containing a vapor compression system.
  • FIGS.l - 3 for further discussion of the vapor compression system, which includes a compressor 14, a downstream heat exchanger 16, an expansion device 18 and an evaporator 20.
  • Compressor 14 is operative to drive a refrigerant along refrigerant lines (FIG.3) first to heat exchanger 16, then to expansion device 18, and then to evaporator 20. Refrigerant flows from evaporator 20 back to compressor 14 to complete the circuit.
  • refrigerant lines FIG.3
  • first heat exchanger 16 is provided having a first heat exchange component 22 and a second heat exchange component 24. These components are positioned within housing 12 to take advantage of the spaces available such that high amounts of heat exchange can be accomplished with relatively small available spaces.
  • housing 12 defines a flow path for heat exchange medium, for example air, to enter into heat exchange relationship with first heat exchanger 16.
  • An upper portion of housing 12 also defines a flow path for air from within the refrigerated space (not shown, but located above housing 12 and supplied with air cooled by arrows 27) to be treated with second heat exchanger 20.
  • extended area of heat exchange contact between the heat exchange medium and the refrigerant-carrying heat exchangers is critical to obtaining good efficiency of the system. It has also been found that such systems operate most efficiently with counter- current flow of refrigerant verses heat exchange medium.
  • first and second components 22, 24 of first heat exchanger 16 can and most likely will be different in size and/or shape so that these components can advantageously take advantage of the available space within a particular device.
  • first component 22 has a relatively larger area in a transverse plane with respect to the flow, and is relatively thin from front to back.
  • first component 22 in this embodiment is sized to fit within a relatively narrow (from front to back) space toward the open front of housing 12.
  • a second space within housing 12 in this embodiment is available beneath a wall 28 which separates one portion of housing 12 for treating the first flow of air 26 from a second portion of housing 12 for treating the second portion of air 27.
  • This wall 28 extends downwardly relative to the outer contour of housing 12, and results in a restriction in flow area as air flows from the inlet end 30 to the outlet end 32 of housing 12.
  • This zone of decreased cross sectional flow area results in an increase in velocity of the air flowing through this zone.
  • An increased velocity flow has been found to provide improved efficiency heat exchange in heat exchangers such as that of the present invention.
  • second component 24 of first heat exchanger 16 it is preferred to position second component 24 of first heat exchanger 16 within this zone of decreased cross sectional flow area so as to take advantage of the increased flow of velocity in this zone:
  • the shape of this zone dictates a different configuration for second component 24 as compared to first component 22.
  • this zone has a substantially short height and yet extends much further from the inlet side toward the outlet side as compared to the space for accommodating first component 22.
  • second component 24 is advantageously shaped and adapted to fit properly within this space, thereby providing maximum possible heat exchange area and further taking advantage of the increased flow velocity of air through that zone.
  • one preferred implementation of the vapor compression system in accordance with the present invention is a transcritical vapor compression system.
  • a transcritical vapor compression system operates upon a refrigerant which does not condense in the first heat exchanger.
  • a refrigerant of a transcritical vapor compression system is CO 2 .
  • other refrigerants could be used well within the scope of the present invention to provide suitable vapor compression systems which would benefit from the heat exchanger arrangement of the present invention.
  • Expansion device 18 can be any suitable expansion device for decreasing the pressure of refrigerant passing there through as is known to a person of skill in the art. Various known expansion devices could be utilized for this purpose.
  • a pressure regulator such as that disclosed in a commonly-owned and simultaneously filed PCT Patent Application bearing attorney docket number 05-258-WO and having the title HIGH SIDE PRESSURE REGULATION FOR TRANSCRITICAL VAPOR COMPRESSION SYSTEM, is a particularly desirable type of expansion device for use in connection with the present invention.
  • the term expansion device is considered to include such a pressure regulator.
  • Second heat exchanger 20 which performs the function of an evaporator, is shown as a single heat exchanger in the drawings. It should be appreciated that second heat exchanger 20 could also be provided in a plurality of components, as well, in the event that space for treatment of flow of air from the refrigerated space is particularly small and/or irregularly shaped.
  • FIG. 3 shows refrigerant lines connecting from first heat exchanger 16 to expansion device 18 and then to second heat exchanger or evaporator 20. Refrigerant flows from evaporator 20 back to the suction inlet of compressor 14.
  • the present invention provides for increased heat exchange efficiency due to increase in area of contact between the heat exchanger and the heat exchange medium. It should further be appreciated that the system of the present invention provides for enhanced utilization of space available for heat exchange, thereby providing more efficient operation of a vapor compression system as desired in accordance with the present invention.
  • This concept is especially useful for transcritical vapor compression systems (such as using CO 2 ), where it is critically important for efficiency that the temperature of refrigerant leaving the heat rejecting heat exchanger be as close as possible to the heat sink fluid (typically air) entering the heat exchanger.
  • the individual heat exchanger segments or components could also be circuited to be as counterflow as possible to further enhance this effect.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Abstract

A refrigeration system includes a compressor for driving a refrigerant along a flow path in at least a first mode of system operation; a first heat exchanger along the flow path downstream of the compressor in the first mode; a second heat exchanger along the flow path upstream of the compressor in the first mode; and a pressure regulator or expansion device in the flow path downstream of the first heat exchanger and upstream of the second heat exchanger in the first mode, wherein the first heat exchanger comprises a plurality of heat exchanger components arranged along a flow path of heat exchange fluid for the first heat exchanger. The heat exchanger components can be positioned in smaller available areas within the unit and thereby use space more efficiently.

Description

MULTI-PART HEAT EXCHANGER CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application claims the benefit of the filing date of earlier filed Provisional Application Serial No. 60/663,917 filed March 18, 2005. Further, copending application docket 05-258-WO, entitled HIGH SIDE PRESSURE REGULATION FOR TRANSCRITICAL VAPOR COMPRESSION SYSTEM and filed on even date herewith, and the aforesaid Provisional Application Serial No. 60/663, 917, disclose prior art and inventive cooler systems. The disclosure of said applications is incorporated by reference herein as if set forth at length.
BACKGROUND OF THE INVENTION
[0002] The invention relates to vapor compression systems and, more particularly, to a heat exchanger configuration for such a system.
[0003] In many vapor compression systems, the heat exchanger placement is very much constrained by space. For these applications, the efficiency of the system is often low in comparison to a system with a properly sized heat exchanger due to the large temperature difference between the air and the refrigerant in the heat exchangers. [0004] The need exists for more efficient heat exchange despite space requirements of the system, and it is an object of the invention to provide such a system. [0005] Other objects and advantages will appear herein below.
SUMMARY OF THE INVENTION
[0006] According to the present invention, the foregoing objects and advantages have been attained.
[0007] According to the invention, a refrigeration system is provided which includes a compressor for driving a refrigerant along a flow path in at least a first mode of system operation; a first heat exchanger along the flow path downstream of the compressor in the first mode; a second heat exchanger along the flow path upstream of the compressor in the first mode; and an expansion device in the flow path downstream of the first heat exchanger and upstream of the second heat exchanger in the first mode, wherein the first heat exchanger comprises a plurality of heat exchanger components arranged along a flow path of heat exchange fluid for the first heat exchanger. The heat exchanger components can be positioned in smaller available areas within the unit and thereby use space more efficiently. Further, flow to these heat exchange components can be routed so as to provide counter flow of the heat exchange fluid, for example air, with the refrigerant. In addition, the system of the present invention can be at least partially if not entirely incorporated into a cassette which can be readily interchanged within the existing housing or case of a refrigerator unit to allow replacement of the cassette when needed without replacing the entire unit.
BRIEF DESCRIPTION OF THE DRAWINGS
[0008] A detailed description of preferred embodiments of the invention follows with reference to the attached drawings, wherein:
[0009] FIG. 1 is a perspective view of a system having a multi-part heat exchanger according to the invention;
[0010] FIG. 2 is a schematic illustration of a multi-part heat exchanger system according to the invention; and
[001 Ij FIG.3 illustrates the refrigerant and air flow in a system according to the invention.
DETAILED DESCRIPTION
[0012] The invention relates to a vapor compression system of a refrigerator unit and, more particularly, to the arrangement of a heat exchanger in a vapor compression system, preferably in a transcritical vapor compression system.
[0013] As set forth above, the greater the area of heat exchanger contact with heat exchange medium such as air, the greater the efficiency in operation of a vapor compression system. In accordance with the present invention, greater contact area between the heat exchanger and heat exchange medium is obtained by utilizing all potentially available spaces within a particular vapor compression system to house additional components of a heat exchanger, such that the heat exchanger is implemented in a series or plurality of heat exchange components. In this manner, small available spaces are nevertheless utilized to increase heat exchange efficiency and, therefore, efficiency of the overall system.
[0014] FIG. 1 shows a system in accordance with the present invention. FIG. 1 shows system 10 which, in this particular embodiment, is the vapor compression system for a bottle cooler refrigeration assembly. FIG. 1 shows the lower portion of such an assembly, including a housing 12 containing a vapor compression system. Reference is made to FIGS.l - 3 for further discussion of the vapor compression system, which includes a compressor 14, a downstream heat exchanger 16, an expansion device 18 and an evaporator 20. Compressor 14 is operative to drive a refrigerant along refrigerant lines (FIG.3) first to heat exchanger 16, then to expansion device 18, and then to evaporator 20. Refrigerant flows from evaporator 20 back to compressor 14 to complete the circuit.
[0015] hi accordance with the present invention, first heat exchanger 16 is provided having a first heat exchange component 22 and a second heat exchange component 24. These components are positioned within housing 12 to take advantage of the spaces available such that high amounts of heat exchange can be accomplished with relatively small available spaces.
[0016] As illustrated in the drawings, housing 12 defines a flow path for heat exchange medium, for example air, to enter into heat exchange relationship with first heat exchanger 16. An upper portion of housing 12 also defines a flow path for air from within the refrigerated space (not shown, but located above housing 12 and supplied with air cooled by arrows 27) to be treated with second heat exchanger 20. [0017] In connection with any heat exchange system, and particularly in connection with vapor compression systems which form the preferred embodiment of the present invention, extended area of heat exchange contact between the heat exchange medium and the refrigerant-carrying heat exchangers is critical to obtaining good efficiency of the system. It has also been found that such systems operate most efficiently with counter- current flow of refrigerant verses heat exchange medium. That is, referring to FIG. 3, if heat exchange medium or air is flowing in the direction of arrows 26, it is preferred that refrigerant flow through heat exchanger 16 be in the flow direction shown such that the direction of flow of refrigerant is counter to that of the flow of heat exchange medium. Referring further to FIGS. 1 - 3, it should readily apparent that first and second components 22, 24 of first heat exchanger 16 can and most likely will be different in size and/or shape so that these components can advantageously take advantage of the available space within a particular device. For example, in the embodiment shown, first component 22 has a relatively larger area in a transverse plane with respect to the flow, and is relatively thin from front to back. This is because first component 22 in this embodiment is sized to fit within a relatively narrow (from front to back) space toward the open front of housing 12. A second space within housing 12 in this embodiment is available beneath a wall 28 which separates one portion of housing 12 for treating the first flow of air 26 from a second portion of housing 12 for treating the second portion of air 27. This wall 28 extends downwardly relative to the outer contour of housing 12, and results in a restriction in flow area as air flows from the inlet end 30 to the outlet end 32 of housing 12. This zone of decreased cross sectional flow area results in an increase in velocity of the air flowing through this zone. An increased velocity flow has been found to provide improved efficiency heat exchange in heat exchangers such as that of the present invention. According to the invention, it is preferred to position second component 24 of first heat exchanger 16 within this zone of decreased cross sectional flow area so as to take advantage of the increased flow of velocity in this zone: Further, the shape of this zone dictates a different configuration for second component 24 as compared to first component 22. Specifically, this zone has a substantially short height and yet extends much further from the inlet side toward the outlet side as compared to the space for accommodating first component 22. Thus, second component 24 is advantageously shaped and adapted to fit properly within this space, thereby providing maximum possible heat exchange area and further taking advantage of the increased flow velocity of air through that zone.
[0018] As set forth above, one preferred implementation of the vapor compression system in accordance with the present invention is a transcritical vapor compression system. Such a system, as is known to a person of skill in the art, operates upon a refrigerant which does not condense in the first heat exchanger. One example of a refrigerant of a transcritical vapor compression system is CO2. Of course, other refrigerants could be used well within the scope of the present invention to provide suitable vapor compression systems which would benefit from the heat exchanger arrangement of the present invention.
[0019] Expansion device 18 can be any suitable expansion device for decreasing the pressure of refrigerant passing there through as is known to a person of skill in the art. Various known expansion devices could be utilized for this purpose. In accordance with a preferred aspect of the present invention, a pressure regulator such as that disclosed in a commonly-owned and simultaneously filed PCT Patent Application bearing attorney docket number 05-258-WO and having the title HIGH SIDE PRESSURE REGULATION FOR TRANSCRITICAL VAPOR COMPRESSION SYSTEM, is a particularly desirable type of expansion device for use in connection with the present invention. As used herein, the term expansion device is considered to include such a pressure regulator.
[0020] Second heat exchanger 20, which performs the function of an evaporator, is shown as a single heat exchanger in the drawings. It should be appreciated that second heat exchanger 20 could also be provided in a plurality of components, as well, in the event that space for treatment of flow of air from the refrigerated space is particularly small and/or irregularly shaped.
[0021] FIG. 3 shows refrigerant lines connecting from first heat exchanger 16 to expansion device 18 and then to second heat exchanger or evaporator 20. Refrigerant flows from evaporator 20 back to the suction inlet of compressor 14. [0022] It should be appreciated that the present invention provides for increased heat exchange efficiency due to increase in area of contact between the heat exchanger and the heat exchange medium. It should further be appreciated that the system of the present invention provides for enhanced utilization of space available for heat exchange, thereby providing more efficient operation of a vapor compression system as desired in accordance with the present invention.
[0023] In some systems it is possible to use a heat exchanger divided into multiple parts and arranged where space is available to increase the overall heat transfer area of the heat exchanger. This disclosure makes use of this with the addition of arranging the multiple parts of the heat exchanger in such a way that the effective refrigerant flows and air (or other heat transfer mediums) flows are opposite to each other. IUU24] FlG. 2 shows an example with a two part heat exchanger. In this case the refrigerant flow would be circuited first through component 24 and then through component 22 if the air flow was directed from front to back. The refrigerant flow would be circuited first through component 22 and then through component 24 if the air flow was from back to front. This concept is especially useful for transcritical vapor compression systems (such as using CO2), where it is critically important for efficiency that the temperature of refrigerant leaving the heat rejecting heat exchanger be as close as possible to the heat sink fluid (typically air) entering the heat exchanger. The individual heat exchanger segments or components could also be circuited to be as counterflow as possible to further enhance this effect.
[0025] In FIG. 2, only one fan 34 is used to move the heat transfer fluid (air) through all of the heat exchanger components 22, 24. This is an additional benefit to cost and energy efficiency, although this is not a necessary embodiment. [0026] The segments or components of the heat exchanger could be manufactured and shipped as one piece, or separately manufactured and connected during the unit assembly process. This type of a heat exchanger is particularly useful for applications where a low number of fins are used on the heat exchanger for reasons of fouling. The reduction in fins due to fouling concerns is offset by the additional heat exchanger tube or channel surface area. This heat exchanger could be a round tube plate fin, wire on tube, microchannel, or any other configuration.
[0027] One or more embodiments of the present invention have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the invention. For example, when implemented as a remanufacturing of an existing system or reengineering of an existing system configuration, details of the existing configuration may influence details of the implementation. Accordingly, other embodiments are within the scope of the following claims.

Claims

CLAIMS What is claimed is:
1. A refrigeration system comprising: a compressor for driving a refrigerant along a flow path in at least a first mode of system operation; a first heat exchanger along the flow path downstream of the compressor in the first mode; a second heat exchanger along the flow path upstream of the compressor in the first mode; and an expansion device in the flow path downstream of the first heat exchanger and upstream of the second heat exchanger in the first mode, wherein the first heat exchanger comprises a plurality of heat exchanger components arranged along a flow path of heat exchange fluid for the first heat exchanger.
2. The system of claim 1 wherein the flow path of the heat exchange fluid is counter to the flow of refrigerant in the heat exchange components.
3. The system of claim 1 wherein the second heat exchanger also comprises a plurality of heat exchange components.
4. The system of claim 1 wherein the first heat exchanger is mounted within a housing having separate and discrete available spaces, and wherein the heat exchanger components are positioned in the spaces.
5. The system of claim 1 further comprising a refrigerator housing defining a cassette receiving area, and wherein the heat exchanger components are mounted within a cassette adapted to be inserted into the receiving area.
6. The system of claim 1, wherein the heat exchanger components include at least a first component and a second component, and wherein the first component has a different shape than the second component.
7. The system of claim 1, wherein the first heat exchanger is mounted within a housing defining a flow path for heat exchanger medium to flow past the first heat exchanger, and wherein the flow path has a cross sectional flow area and a decreased flow area zone along the path, and wherein at least one of the components is positioned at the decreased flow area zone.
8. The system of claim 1, wherein the refrigerant comprises, in major mass part, CO2; and the first and second heat exchangers are refrigerant-air heat exchangers.
9. The system of claim 1, wherein the system contains a refrigerant and the refrigerant is a transcritical vapor compression.
10. A beverage cooling device comprising the system of claim 1.
PCT/US2005/047524 2005-03-18 2005-12-30 Multi-part heat exchanger Ceased WO2006101563A2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
HK08111972.1A HK1120103B (en) 2005-03-18 2005-12-30 Multi-part heat exchanger
US11/908,418 US20080184731A1 (en) 2005-03-18 2005-12-30 Multi-Part Heat Exchanger
JP2008501863A JP4705157B2 (en) 2005-03-18 2005-12-30 Multi-element heat exchanger
ES05856004.6T ES2580080T3 (en) 2005-03-18 2005-12-30 Multi-part heat exchanger
EP05856004.6A EP1872068B1 (en) 2005-03-18 2005-12-30 Multi-part heat exchanger

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US9175203B2 (en) 2009-09-11 2015-11-03 Arkema France Ternary compositions for low-capacity refrigeration
US9267064B2 (en) 2009-09-11 2016-02-23 Arkema France Ternary compositions for high-capacity refrigeration
US9599381B2 (en) 2008-10-08 2017-03-21 Arkema France Heat transfer fluid
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US9663697B2 (en) 2009-09-11 2017-05-30 Arkema France Use of ternary compositions
US9683157B2 (en) 2009-09-11 2017-06-20 Arkema France Heat transfer method
US9267064B2 (en) 2009-09-11 2016-02-23 Arkema France Ternary compositions for high-capacity refrigeration
US9399726B2 (en) 2009-09-11 2016-07-26 Arkema France Use of ternary compositions
US9505968B2 (en) 2009-09-11 2016-11-29 Arkema France Ternary compositions for low-capacity refrigeration
US9133379B2 (en) 2009-09-11 2015-09-15 Arkema France Binary refrigerating fluid
US9039922B2 (en) 2009-09-11 2015-05-26 Arkema France Low-temperature and average-temperature refrigeration
US9175203B2 (en) 2009-09-11 2015-11-03 Arkema France Ternary compositions for low-capacity refrigeration
US9884984B2 (en) 2009-09-11 2018-02-06 Arkema France Binary refrigerating fluid
US10035938B2 (en) 2009-09-11 2018-07-31 Arkema France Heat transfer fluid replacing R-134a
US10125296B2 (en) 2009-09-11 2018-11-13 Arkema France Binary refrigerating fluid
US10316231B2 (en) 2009-09-11 2019-06-11 Arkema France Low-temperature and average-temperature refrigeration
US10358592B2 (en) 2009-09-11 2019-07-23 Arkema France Heat transfer method
US10858562B2 (en) 2009-09-11 2020-12-08 Arkema France Binary refrigerating fluid
US9127191B2 (en) 2009-09-11 2015-09-08 Arkema France Use of ternary compositions

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EP1872068B1 (en) 2016-06-22
JP4705157B2 (en) 2011-06-22
EP1872068A4 (en) 2011-11-16
US20080184731A1 (en) 2008-08-07
CN100575813C (en) 2009-12-30
WO2006101563A3 (en) 2008-01-17
HK1120103A1 (en) 2009-03-20
ES2580080T3 (en) 2016-08-19
CN101175952A (en) 2008-05-07
EP1872068A2 (en) 2008-01-02
JP2008533425A (en) 2008-08-21

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