EP1260776B1 - A heat exchanger for an air conditioning system - Google Patents

A heat exchanger for an air conditioning system Download PDF

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Publication number
EP1260776B1
EP1260776B1 EP01112491A EP01112491A EP1260776B1 EP 1260776 B1 EP1260776 B1 EP 1260776B1 EP 01112491 A EP01112491 A EP 01112491A EP 01112491 A EP01112491 A EP 01112491A EP 1260776 B1 EP1260776 B1 EP 1260776B1
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EP
European Patent Office
Prior art keywords
refrigerant
pathway
flow
bypass
heat exchanger
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Expired - Lifetime
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EP01112491A
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German (de)
French (fr)
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EP1260776A1 (en
Inventor
Thomas Tiedemann
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Valeo Thermal Systems Japan Corp
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Zexel Valeo Climate Control Corp
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Priority to EP01112491A priority Critical patent/EP1260776B1/en
Priority to DE60125146T priority patent/DE60125146T2/en
Publication of EP1260776A1 publication Critical patent/EP1260776A1/en
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Publication of EP1260776B1 publication Critical patent/EP1260776B1/en
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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
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/04Refrigeration circuit bypassing means
    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/05Compression system with heat exchange between particular parts of the system
    • F25B2400/054Compression system with heat exchange between particular parts of the system between the suction tube of the compressor and another part of the cycle
    • 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
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2501Bypass valves
    • 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
    • F25B41/00Fluid-circulation arrangements
    • F25B41/20Disposition of valves, e.g. of on-off valves or flow control valves
    • 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

Definitions

  • the present invention relates to a heat exchanger for an air conditioning system and in particular for a CO 2 air conditioning system for use in an automotive vehicle.
  • CO 2 carbon dioxide
  • R134a tetrafluoroethane
  • Fig. 1 is a diagram of a conventional cold-vapour refrigeration cycle wherein a refrigerant is circulated in a closed circuit made up of a compressor 1, a first heat exchanger in the form of a condenser 2, an expansion valve 3 and a second heat exchanger in the form of an evaporator 4.
  • the refrigerant which is under low pressure is evaporated into a gaseous phase in the evaporator 4, which typically comprising a coiled pipe.
  • the evaporation lowers the temperature of the air passing over the evaporator 4, for example for use in a vehicle air conditioning system, such air being that which is blown into the passenger compartment of the vehicle.
  • the compressor 2 draws away the refrigerant from the evaporator 4, compresses it and passes it to the condenser 2, where the refrigerant gives up its heat to the environment, and as a result of its increased pressure and loss of heat condenses back to a liquid phase. It may even become supercooled. Finally, the liquid refrigerant is expanded to a lower vaporizing pressure via the expansion valve 3 and returned to the evaporator 4.
  • the refrigeration cycle in this device comprises a compressor 10, a gas cooler 11, a counter-current heat exchanger 12, an expansion valve 13, an evaporator 14, a combination liquid separator and accumulator 16, and a return flow through the internal counter-current hear exchanger 12 to the compressor 10.
  • the internal counter-current heat exchanger 12 improves the process efficiency and substantially increases the available refrigerating capacity, particularly at high ambient temperatures. It operates by transferring heat from the relatively warm refrigerant discharged from the condenser 11 to the colder refrigerant discharged from the evaporator 14 or the accumulator 16. The refrigerant temperature is thereby lowered prior to expansion via the valve 13 so that the wet vapour content after expansion is decreased and the available refrigerating capacity is thereby increased. However, the heat transfer causes the refrigerant temperature at the inlet to the compressor 10 to increase, which results in a proportional increase in the refrigerant temperature leaving the compressor.
  • the design of the heat exchanger is a compromise between the following two requirements.
  • Documents EP 1 043 550, EP 0 915 306, EP 0 779 481 and US 5,479,789 are directed toward refrigeration cycles, or heat pumps Each document discloses the use of a heat exchanger within the coolant circuitry.
  • Document EP-A-1 043 550 discloses a heat exchanger, a refrigeration system and a method of regulating thermal flow in a refrigeration system according to the preamble of claims 1, 6 and 8 respectively. None of the documents, however, discloses the use of a valve positioned at either the inlet or the outlet to a bypass provided on the paths through the heat exchanger. Such positioning of the valves, allows that the coolant flow can be fully controlled and ultimately stopped from passing through the heat exchanger.
  • the object of the present invention is to provide an internal heat exchanger for use in a vehicle air conditioning system in which the thermal flow is substantially maximized under all operating conditions of the air conditioning system whilst the final compression temperature is maintained within permitted limits.
  • the present invention is detailed in claim 1, with further embodiments given in dependent claims thereof.
  • the heat exchanger for use in a refrigeration system of a vehicle air conditioning system according to claim 1 defines a first refrigerant pathway through which refrigerant can flow from a gas cooler of the system to an expansion valve of the system.
  • a second refrigerant pathway through which the refrigerant can flow from an evaporator or accumulator of the system to a compressor of the system is also given.
  • the two pathways are arranged so that a thermal flow can occur between the refrigerant flowing in the first and second pathways.
  • a first and/or second bypass are provided through which at least a portion of the refrigerant can flow instead of flowing through at least one of the first pathway, the second pathway.
  • a control valve is provided at a branch-off point in the first or second pathway at an inlet or an outlet to the first or second bypass respectively, whereby refrigerant flow through both the first or second bypass and the first or second pathway provided with the first of second bypass can be controlled, and the flow through either the first or second pathway can be stopped.
  • a heat exchanger 12 for use in a refrigeration cycle of a vehicle air conditioning system as described above with reference to Fig. 2 comprises a first refrigerant pathway 20 through which high-pressure refrigerant can flow from the condenser 11 of the refrigeration system to the expansion valve 13 and a second refrigerant pathway 21 through which low-pressure refrigerant can flow from the evaporator 14 or the accumulator 16 to the compressor 10.
  • the two pathways 20, 21 are arranged in a conventional manner so that a thermal flow can occur between the refrigerant flowing in them.
  • the pathways 20, 21 are arranged in a manner which would maximize the thermal flow.
  • a bypass 22 is provided through which refrigerant can flow instead of flowing through at least one of the pathways 20, 21.
  • the first pathway 20 is provided with the bypass but a similar bypass 23 could be provided for the second pathway, as shown in Fig. 4, in addition to or in place of the bypass 22.
  • a control valve V1 is provided in order to control the flow of refrigerant through the bypass 22 or the bypass 23. As shown in Fig. 3, when the control valve V1 closes the bypass 22, all of the refrigerant flows through the pathway 20 and in this case the thermal flow between the pathways 20 and 21 is maximized.
  • control valve V1 When the thermal flow is to be reduced, the control valve V1 is operated to reduce the high-pressure side flow of refrigerant through the pathway 20 by permitting flow through the bypass 22. In extreme cases the flow through the pathway 20 can be completely stopped so that the refrigerant flows solely through the bypass 22. In this case the refrigeration cycle operates in a manner as described with reference to Fig. 1 where no internal heat exchanger is present.
  • the control valve V1 can be installed in a variety of positions as shown in Fig. 4. If the control valve is located at a position V1 or V2 on the high-pressure side of the exchanger in the first pathway 20 at the branch-off points for the bypass 22, or similarly at a position V3 or V4 on the low-pressure side of the exchanger in the second pathway 21 at the branch-off points for the bypass 23, then flow of refrigerant through the pathways 20 and 21 as well as through the bypasses 22 and 23 can be directly controlled.
  • the control valve could be located at positions V5 and V6 at intermediate positions within in the bypasses 22 and 23 respectively. This valve arrangement does not fall under the scope of the claims.
  • bypasses 22 and 23 can be directly controlled and, owing to the lower pressures losses of the bypasses 22, 23 as compared to the pathways 20 and 21, nearly the full flow through the heat exchanger may be diverted to the bypasses 22, 23.
  • the advantage of positioning the control valve at positions V5 and V6 is that it permits a less complex valve to be used than would be the case for the other positions.
  • FIG. 5 A modification of a heat exchanger 12 for use in a refrigeration cycle of a vehicle air conditioning system as described above with reference to Fig. 2 is shown in Fig. 5.
  • the heat exchanger comprises a bypass 22 for the first pathway 20 and a plurality of conduits 24 are provided between the bypass 22 and the pathway 20 at spaced intervals along the length of the pathway 20.
  • three such conduits 24a, 24b, 24c are provided, each of which is provided with a control valve Z1, Z2, Z3 respectively to control independently the refrigerant flow therethrough.
  • a further control valve Z4 is provided in the inlet to the bypass 22. This valve arrangement does not fall under the scope of the claims.
  • a first control valve Z1 can be opened to permit refrigerant flow through the conduit 24a so that a major portion of the refrigerant is diverted from the pathway 20 into the bypass 22 through the conduit 24a due to the lower pressure losses, the minor portion of the refrigerant continuing to flow through the pathway 20.
  • the valves Z2 and Z3 may be opened in succession to permit flow through the conduits 24b and 24C thus diverting refrigerant from the pathway 20 at successively earlier stages of the refrigerants travel through the heat exchanger 12. By opening the valve z4, the refrigerant will flow wholly through the bypass 22 and the pathway 20 is then completely bypassed.
  • the variable which is used to control operation of the control valves V1-V6 and Z1-Z4 is the temperature of the refrigerant subsequent to its compression in the compressor 10. If this temperature exceeds a predetermined level, then the control valves V1-V6 and Z1-Z4 are set to operate to increase the flow of refrigerant through the bypass 22, 23 so that the thermal flow between the pathways 20 and 21 is reduced. The final compression temperature is thereby also reduced. However, owing to the interrelationship between the temperature of the refrigerant both before and after compression, it is also possible to use the temperature of the refrigerant prior to compression as the control variable.
  • valves V1 to V4 in Fig. 4 may be arranged to correspond with the controller of the cooling water circuit of the vehicle as in both cases a mass flow of fluid is distributed to two circuits dependent on the operating temperature.
  • valves V5 and V6 and of the valves Z1 to Z4 is simpler because only one mass flow of fluid is controlled dependent on the operating temperature.
  • Conventional thermostatic expansion valves as used in air-conditioning and refrigerating engineering, or valves of this type, can be used for these valves.

Description

  • The present invention relates to a heat exchanger for an air conditioning system and in particular for a CO2 air conditioning system for use in an automotive vehicle.
  • The use of carbon dioxide (CO2) as a refrigerant is being investigated widely to replace tetrafluoroethane (R134a) as the refrigerant in the air conditioning systems of automotive vehicles. However, unlike the more conventional refrigerants such as R134a, CO2 has a low critical temperature so that a trans-critical process must be employed.
  • Fig. 1 is a diagram of a conventional cold-vapour refrigeration cycle wherein a refrigerant is circulated in a closed circuit made up of a compressor 1, a first heat exchanger in the form of a condenser 2, an expansion valve 3 and a second heat exchanger in the form of an evaporator 4. The refrigerant, which is under low pressure is evaporated into a gaseous phase in the evaporator 4, which typically comprising a coiled pipe. The evaporation lowers the temperature of the air passing over the evaporator 4, for example for use in a vehicle air conditioning system, such air being that which is blown into the passenger compartment of the vehicle. The compressor 2 draws away the refrigerant from the evaporator 4, compresses it and passes it to the condenser 2, where the refrigerant gives up its heat to the environment, and as a result of its increased pressure and loss of heat condenses back to a liquid phase. It may even become supercooled. Finally, the liquid refrigerant is expanded to a lower vaporizing pressure via the expansion valve 3 and returned to the evaporator 4.
  • This cycle could be used with refrigerants such as CO2 in which heat is given off under supercritical conditions. EP 0,424,474 describes a trans-critical vapour compression cycle device suitable for use with CO2 as the refrigerant wherein the specific enthalpy of the refrigerant is regulated at the inlet of the evaporator by the deliberate use of the pressure and/or temperature. As shown in Fig. 2, the refrigeration cycle in this device comprises a compressor 10, a gas cooler 11, a counter-current heat exchanger 12, an expansion valve 13, an evaporator 14, a combination liquid separator and accumulator 16, and a return flow through the internal counter-current hear exchanger 12 to the compressor 10. The internal counter-current heat exchanger 12 improves the process efficiency and substantially increases the available refrigerating capacity, particularly at high ambient temperatures. It operates by transferring heat from the relatively warm refrigerant discharged from the condenser 11 to the colder refrigerant discharged from the evaporator 14 or the accumulator 16. The refrigerant temperature is thereby lowered prior to expansion via the valve 13 so that the wet vapour content after expansion is decreased and the available refrigerating capacity is thereby increased. However, the heat transfer causes the refrigerant temperature at the inlet to the compressor 10 to increase, which results in a proportional increase in the refrigerant temperature leaving the compressor.
  • As the heat transfer area of the solid structural components used in the refrigeration system for the heat exchanger 12 cannot be varied, and as the conditions under which air conditioning systems in vehicles are used varies considerably as a result of variation in the ambient temperatures, the driving speed of the compressor and the desired refrigerating capacity, the design of the heat exchanger is a compromise between the following two requirements.
    1. 1. The requirement to maximize performance and to achieve a high refrigerating capacity, which necessitates the internal heat exchanger transferring the maximum thermal flow possible from the high-pressure side to the low-pressure side of the circuit. The limitations to this are caused by the fact that the temperatures on either side of the heat exchanger approach one another.
    2. 2. The requirement that the optimum operating characteristics of the oil used in the compressor are maintained, which necessitates that the maximum temperature subsequent to compression of the refrigerant and the oil blend used must not exceed an upper permitted temperature. As the temperature of the refrigerant subsequent to compression is determined, inter alia, by its temperature at the start of the compression step, heating of the refrigerant upstream of the compressor 10 within the internal heat exchanger 12 must be limited so as to avoid a high final compression temperature which exceeds the upper permitted temperature.
  • Documents EP 1 043 550, EP 0 915 306, EP 0 779 481 and US 5,479,789 are directed toward refrigeration cycles, or heat pumps Each document discloses the use of a heat exchanger within the coolant circuitry. Document EP-A-1 043 550 discloses a heat exchanger, a refrigeration system and a method of regulating thermal flow in a refrigeration system according to the preamble of claims 1, 6 and 8 respectively. None of the documents, however, discloses the use of a valve positioned at either the inlet or the outlet to a bypass provided on the paths through the heat exchanger. Such positioning of the valves, allows that the coolant flow can be fully controlled and ultimately stopped from passing through the heat exchanger.
  • The object of the present invention is to provide an internal heat exchanger for use in a vehicle air conditioning system in which the thermal flow is substantially maximized under all operating conditions of the air conditioning system whilst the final compression temperature is maintained within permitted limits.
  • The present invention is detailed in claim 1, with further embodiments given in dependent claims thereof. The heat exchanger for use in a refrigeration system of a vehicle air conditioning system according to claim 1 defines a first refrigerant pathway through which refrigerant can flow from a gas cooler of the system to an expansion valve of the system.
  • A second refrigerant pathway through which the refrigerant can flow from an evaporator or accumulator of the system to a compressor of the system is also given. The two pathways are arranged so that a thermal flow can occur between the refrigerant flowing in the first and second pathways. Further a first and/or second bypass are provided through which at least a portion of the refrigerant can flow instead of flowing through at least one of the first pathway, the second pathway.
  • A control valve is provided at a branch-off point in the first or second pathway at an inlet or an outlet to the first or second bypass respectively, whereby refrigerant flow through both the first or second bypass and the first or second pathway provided with the first of second bypass can be controlled, and the flow through either the first or second pathway can be stopped.
  • The present invention will now be described by way of example with reference to the accompanying drawings, in which:-
    • Fig. 1 is a diagram of a conventional cold-vapour refrigeration cycle;
    • Fig. 2 is a diagram of a conventional trans-critical vapour compression refrigerating cycle;
    • Fig. 3 is a schematic diagram of a heat exchanger in accordance with the present invention for use in a refrigerating cycle as shown in Fig. 2;
    • Fig. 4 is a view similar to Fig. 3 showing various locations for the positions of one or more control valves forming part of the heat exchanger; and
    • Fig. 5 is a schematic diagram of a modified heat exchanger;
  • As shown in Fig. 3, a heat exchanger 12 according to the present invention for use in a refrigeration cycle of a vehicle air conditioning system as described above with reference to Fig. 2 comprises a first refrigerant pathway 20 through which high-pressure refrigerant can flow from the condenser 11 of the refrigeration system to the expansion valve 13 and a second refrigerant pathway 21 through which low-pressure refrigerant can flow from the evaporator 14 or the accumulator 16 to the compressor 10. The two pathways 20, 21 are arranged in a conventional manner so that a thermal flow can occur between the refrigerant flowing in them. Preferably, the pathways 20, 21 are arranged in a manner which would maximize the thermal flow.
  • However, in order that the thermal flow between the pathways 20, 21 can be regulated, a bypass 22 is provided through which refrigerant can flow instead of flowing through at least one of the pathways 20, 21. In Fig. 3 the first pathway 20 is provided with the bypass but a similar bypass 23 could be provided for the second pathway, as shown in Fig. 4, in addition to or in place of the bypass 22. In order to control the flow of refrigerant through the bypass 22 or the bypass 23, a control valve V1 is provided. As shown in Fig. 3, when the control valve V1 closes the bypass 22, all of the refrigerant flows through the pathway 20 and in this case the thermal flow between the pathways 20 and 21 is maximized. When the thermal flow is to be reduced, the control valve V1 is operated to reduce the high-pressure side flow of refrigerant through the pathway 20 by permitting flow through the bypass 22. In extreme cases the flow through the pathway 20 can be completely stopped so that the refrigerant flows solely through the bypass 22. In this case the refrigeration cycle operates in a manner as described with reference to Fig. 1 where no internal heat exchanger is present.
  • It will be appreciated that control of the flow of refrigerant on the low-pressure side of the heat exchanger by the use of the bypass 23 and associated control valve would have the same effect.
  • The control valve V1 can be installed in a variety of positions as shown in Fig. 4. If the control valve is located at a position V1 or V2 on the high-pressure side of the exchanger in the first pathway 20 at the branch-off points for the bypass 22, or similarly at a position V3 or V4 on the low-pressure side of the exchanger in the second pathway 21 at the branch-off points for the bypass 23, then flow of refrigerant through the pathways 20 and 21 as well as through the bypasses 22 and 23 can be directly controlled. However, the control valve could be located at positions V5 and V6 at intermediate positions within in the bypasses 22 and 23 respectively. This valve arrangement does not fall under the scope of the claims. In this case only the flow through the bypasses 22 and 23 can be directly controlled and, owing to the lower pressures losses of the bypasses 22, 23 as compared to the pathways 20 and 21, nearly the full flow through the heat exchanger may be diverted to the bypasses 22, 23. The advantage of positioning the control valve at positions V5 and V6 is that it permits a less complex valve to be used than would be the case for the other positions.
  • A modification of a heat exchanger 12 for use in a refrigeration cycle of a vehicle air conditioning system as described above with reference to Fig. 2 is shown in Fig. 5. Here the heat exchanger comprises a bypass 22 for the first pathway 20 and a plurality of conduits 24 are provided between the bypass 22 and the pathway 20 at spaced intervals along the length of the pathway 20. In the illustrated embodiment three such conduits 24a, 24b, 24c are provided, each of which is provided with a control valve Z1, Z2, Z3 respectively to control independently the refrigerant flow therethrough. A further control valve Z4 is provided in the inlet to the bypass 22. This valve arrangement does not fall under the scope of the claims.
  • When the thermal flow between the pathways 20 and 21 is to be reduced, a first control valve Z1 can be opened to permit refrigerant flow through the conduit 24a so that a major portion of the refrigerant is diverted from the pathway 20 into the bypass 22 through the conduit 24a due to the lower pressure losses, the minor portion of the refrigerant continuing to flow through the pathway 20. If it is desired to reduce the thermal flow still further, the valves Z2 and Z3 may be opened in succession to permit flow through the conduits 24b and 24C thus diverting refrigerant from the pathway 20 at successively earlier stages of the refrigerants travel through the heat exchanger 12. By opening the valve z4, the refrigerant will flow wholly through the bypass 22 and the pathway 20 is then completely bypassed.
  • It will be appreciated that an equivalent arrangement could be provided which controls an inflow of refrigerant to the pathway 20 from the bypass 22 rather than an outflow of refrigerant from the pathway 20 as described above.
  • The variable which is used to control operation of the control valves V1-V6 and Z1-Z4 is the temperature of the refrigerant subsequent to its compression in the compressor 10. If this temperature exceeds a predetermined level, then the control valves V1-V6 and Z1-Z4 are set to operate to increase the flow of refrigerant through the bypass 22, 23 so that the thermal flow between the pathways 20 and 21 is reduced. The final compression temperature is thereby also reduced. However, owing to the interrelationship between the temperature of the refrigerant both before and after compression, it is also possible to use the temperature of the refrigerant prior to compression as the control variable.
  • In a vehicle air conditioning system, the configuration of the valves V1 to V4 in Fig. 4 may be arranged to correspond with the controller of the cooling water circuit of the vehicle as in both cases a mass flow of fluid is distributed to two circuits dependent on the operating temperature. However, the design of valves V5 and V6 and of the valves Z1 to Z4 is simpler because only one mass flow of fluid is controlled dependent on the operating temperature. Conventional thermostatic expansion valves as used in air-conditioning and refrigerating engineering, or valves of this type, can be used for these valves.

Claims (8)

  1. A heat exchanger (12) for use in a refrigeration system of a vehicle air conditioning system defining a first refrigerant pathway (20) through which refrigerant can flow from a gas cooler (11) of the system to an expansion valve (13) of the system; and
    a second refrigerant pathway (21) through which the refrigerant can flow from an evaporator (14) or accumulator (16) of the system to a compressor (10) of the system, the two pathways (20, 21) being arranged so that a thermal flow can occur between the refrigerant flowing in the first and second pathways (20, 21), and
    a first and/or second bypass (22, 23) is provided through which at least a portion of the refrigerant can flow instead of flowing through at least one of the first pathway (20), the second pathway (21),
    characterized in that
    a control valve (V1 - V4) is provided at a branch-off point in the first or second pathway (20, 21) at an inlet or an outlet to the first or second bypass (22, 23) respectively, whereby refrigerant flow through both the first or second bypass (22, 23) and the first or second pathway (20, 21) provided with the first or second bypass (22, 23) can be controlled, and the flow through either the first or second pathway (20, 21) can be stopped.
  2. A heat exchanger as claimed in Claim 1, characterised in that the first bypass (22) is provided for the first pathway (20).
  3. A heat exchanger as claimed in any of Claims 1 or 2, characterised in that the second bypass (23) is provided for the second pathway (21).
  4. A heat exchanger as claimed in any one of Claims 1 to 3, characterised in that first and second bypasses (22, 23) are provided for the first and the second pathways (20, 21) respectively.
  5. A heat exchanger as claimed in any one of Claims 1 to 4, characterised in that a controller is provided which controls the opening and closing of the control valve (V1, V2, V3, V4).
  6. A refrigeration system for a vehicle air conditioning system comprising a compressor (10), a gas cooler (11), an expansion valve (13), an evaporator (14), and an internal heat exchanger (12) connected in series to form an integral closed circuit, the internal heat exchanger (12) defining a first refrigerant pathway (20) through which refrigerant can flow from the condenser (11) to the expansion valve (13) and a second refrigerant (21) pathway through which the refrigerant can flow from the evaporator (14) to the compressor (10), the two pathways (20, 21) being arranged so that a thermal flow can occur between the refrigerant flowing in the pathways (20, 21), and
    a first and/or second bypass (22, 23) is provided through which refrigerant can flow instead of flowing through at least one of the first pathway (20) and the second pathway (21),
    characterized in that
    a control valve (V1 - V4) is provided at a branch-off point in the first or second pathway (20, 21) at an inlet or an outlet to the first or second bypass (22, 23) respectively, whereby refrigerant flow through both the first or second bypass (22, 23) and the first or second pathway (20, 21) provided with the first or second bypass (22, 23) can be controlled, and the flow through either the first or second pathway (20, 21) can be stopped.
  7. A system as claimed in Claim 6, characterised in that the refrigerant is carbon dioxide.
  8. A method of regulating thermal flow in a refrigeration system for a vehicle air conditioning system, comprising the steps of evaporating a refrigerant into a gaseous phase in an evaporator (14) and passing it to a compressor (10);
    compressing a gaseous refrigerant in the compressor (10);
    passing the gaseous refrigerant to a gas cooler (11) where the refrigerant is permitted to give up its heat to the environment expanding the refrigerant to a lower vaporizing pressure via an expansion valve (13);
    returning the refrigerant to the evaporator (14); and
    passing the gaseous refrigerant through an internal heat exchanger (12) in order that a thermal flow can occur between the refrigerant flowing in a first pathway (20) located intermediate the gas cooler (11) and the expansion valve (13) and the refrigerant flowing in a second pathway (21) located intermediate the evaporator (14) and the compressor (10); whereby
    a first and/or second bypass (22, 23) is provided through which refrigerant can flow instead of flowing through at least one of the first pathway (20) and the second pathway (21),
    characterized by
    controlling the refrigerant flow through both the first/second bypass (22, 23) and the first/second pathway (20, 21) provided with the bypass by a control valve (V1, V2, V3, V4) provided at a branch-off point in the first/second pathway (20, 21) provided with the first/second bypass (22, 23) and the flow through the first/second pathway (20, 21) can be stopped.
EP01112491A 2001-05-22 2001-05-22 A heat exchanger for an air conditioning system Expired - Lifetime EP1260776B1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP01112491A EP1260776B1 (en) 2001-05-22 2001-05-22 A heat exchanger for an air conditioning system
DE60125146T DE60125146T2 (en) 2001-05-22 2001-05-22 Heat exchanger for air conditioning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP01112491A EP1260776B1 (en) 2001-05-22 2001-05-22 A heat exchanger for an air conditioning system

Publications (2)

Publication Number Publication Date
EP1260776A1 EP1260776A1 (en) 2002-11-27
EP1260776B1 true EP1260776B1 (en) 2006-12-13

Family

ID=8177512

Family Applications (1)

Application Number Title Priority Date Filing Date
EP01112491A Expired - Lifetime EP1260776B1 (en) 2001-05-22 2001-05-22 A heat exchanger for an air conditioning system

Country Status (2)

Country Link
EP (1) EP1260776B1 (en)
DE (1) DE60125146T2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7114349B2 (en) * 2004-12-10 2006-10-03 Carrier Corporation Refrigerant system with common economizer and liquid-suction heat exchanger
CN103851853A (en) * 2014-03-28 2014-06-11 合肥华凌股份有限公司 Heat exchanger and refrigerator using same
CN116222043A (en) * 2021-12-03 2023-06-06 青岛海尔特种电冰柜有限公司 Control method of refrigerating device

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5479789A (en) * 1994-12-29 1996-01-02 Aire Solutions, Inc. Heat exchanger for a heat pump
JP3538492B2 (en) * 1995-12-15 2004-06-14 昭和電工株式会社 Refrigeration cycle device
US6105386A (en) * 1997-11-06 2000-08-22 Denso Corporation Supercritical refrigerating apparatus
JPH11193967A (en) * 1997-12-26 1999-07-21 Zexel:Kk Refrigerating cycle
JP2000346472A (en) * 1999-06-08 2000-12-15 Mitsubishi Heavy Ind Ltd Supercritical steam compression cycle
DE19944951B4 (en) * 1999-09-20 2010-06-10 Behr Gmbh & Co. Kg Air conditioning with internal heat exchanger

Also Published As

Publication number Publication date
EP1260776A1 (en) 2002-11-27
DE60125146D1 (en) 2007-01-25
DE60125146T2 (en) 2007-04-12

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