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JP2009008383A - Co2 refrigeration system having heat pump and multiple modes of operation - Google Patents

Co2 refrigeration system having heat pump and multiple modes of operation Download PDF

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Publication number
JP2009008383A
JP2009008383A JP2008150515A JP2008150515A JP2009008383A JP 2009008383 A JP2009008383 A JP 2009008383A JP 2008150515 A JP2008150515 A JP 2008150515A JP 2008150515 A JP2008150515 A JP 2008150515A JP 2009008383 A JP2009008383 A JP 2009008383A
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Prior art keywords
refrigerant
refrigerant circuit
cooling system
heat exchanger
evaporator
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JP2008150515A
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Japanese (ja)
Inventor
Jianmin Yin
ジアンミン・イン
Michael J Wilson
マイケル・ジェイ・ウィルソン
Stephen B Memory
スティーブン・ビー・メモリー
Samuel J Collier
サミュエル・ジェイ・コリアー
Todd M Bandhauer
トッド・エム・バンドハウアー
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Modine Manufacturing Co
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Modine Manufacturing Co
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    • 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
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/003Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
    • 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
    • F25B5/00Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
    • F25B5/04Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity 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
    • 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
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/047Water-cooled condensers
    • 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
    • F25B25/00Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
    • F25B25/005Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00 using primary and secondary systems
    • 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
    • F25B27/00Machines, plants or systems, using particular sources of energy
    • F25B27/02Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
    • 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
    • F25B6/00Compression machines, plants or systems, with several condenser circuits
    • F25B6/04Compression machines, plants or systems, with several condenser circuits arranged in series
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine

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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)
  • Air-Conditioning For Vehicles (AREA)
  • Cooling Or The Like Of Electrical Apparatus (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a CO<SB>2</SB>heat pump system and its manufacturing method without causing the practical problem such as requiring a valve capable of coping with high pressure CO<SB>2</SB>, an accumulator of a proper size and a system inside heat exchanger endurable against high system pressure in a whole reversible system. <P>SOLUTION: While a refrigeration system 10 is operated in an air-conditioning or cooling (A/C) mode, CO<SB>2</SB>of a refrigerant enters a first evaporator 14 from a compressor 12, and then, enters a second evaporator 18. A liquid coolant flows through a second coolant loop 19, and further lowers the refrigerant temperature, but a heat load of the second evaporator 18 can be reduced more than that of the air-cooled first evaporator 14. The refrigerant coming out of the second evaporator flows in the high pressure side of a suction line inside heat exchanger 20 before turning to an expansion device or an expansion valve 22, and flows in an air to refrigerant type evaporator 24 after coming out of the expansion valve 22. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本件出願は2007年6月8日に出願された米国仮特許出願番号第60/933,713号の優先権を主張するものである。
本発明は冷却システムに関し、詳しくは、空気加熱モード又はヒートポンプモード及び空調モード又は冷却モードの何れをも有する遷臨界システム又はCO2冷却システムに関する。
This application claims priority from US Provisional Patent Application No. 60 / 933,713, filed June 8, 2007.
The present invention relates to a cooling system, and more particularly, to a transcritical system or a CO 2 cooling system having both an air heating mode or a heat pump mode and an air conditioning mode or a cooling mode.

CO2ヒートポンプシステムはその原理上、A/Cモード蒸発器をHPモードガスクーラーとして動作させ、A/CモードガスクーラーをHPモード蒸発器として動作させるようにシステムサイクル内での流れ方向を変えてやることで、ヒートポンプモード又は加熱(HP)モードから空調モード又は冷却(A/C)モードに切り換えることができる。しかしながらこの方法には、これに限定しないが、高圧のCO2に対処し得る弁、適宜サイズのアキュムレーター、全可逆システムにおける高いシステム圧力に耐え得るシステム内熱交換器が必要となる、といった幾つかの実用上の問題がある。 In principle, the CO 2 heat pump system changes the flow direction in the system cycle so that the A / C mode evaporator operates as an HP mode gas cooler and the A / C mode gas cooler operates as an HP mode evaporator. By doing so, it is possible to switch from the heat pump mode or the heating (HP) mode to the air conditioning mode or the cooling (A / C) mode. However, this method requires, but is not limited to, a valve that can handle high pressure CO 2 , an appropriately sized accumulator, and an in-system heat exchanger that can withstand the high system pressure in a fully reversible system. There are some practical problems.

米国仮特許出願番号第60/933,713号US Provisional Patent Application No. 60 / 933,713

高圧のCO2に対処し得る弁、適宜サイズのアキュムレーター、全可逆システムにおける高いシステム圧力に耐え得るシステム内熱交換器が必要となる、といった実用上の問題の無いCO2ヒートポンプシステム及びその製造方法を提供することである。 A CO 2 heat pump system that does not require practical problems such as a valve that can cope with high-pressure CO 2 , an appropriately sized accumulator, and an in-system heat exchanger that can withstand high system pressure in a fully reversible system, and its manufacture Is to provide a method.

本発明によれば、冷却材ループを二重化し、熱交換器を増設することにより、システム内での冷媒の流れ方向を変えずにHP及びA/Cの両モード下に動作させ得るようにした冷却システムが提供される。本冷却システムは、エンジン停止状態のトラックの車室の冷暖房用途で使用するのが望ましい。ある実施例ではCO2が少なくとも1つの冷媒回路内で冷媒として使用される。
ある実施例では本発明は、荷室を加熱する加熱モードと、荷室を除熱する冷却モードの何れをも備える冷却システムを提供する。本冷却システムには第1、第2、及び第3の各冷媒回路が含まれ、第1冷媒回路は、この第1冷媒回路の冷媒の熱を空気に移行させる第1熱交換器を含み、第2冷媒回路は、空気の熱をこの第2冷媒回路に移行させる第2熱交換器を含む。第3冷媒回路は、この第3冷媒回路の冷媒の圧力を増大させるためのコンプレッサと、このコンプレッサから冷媒を受けるべくコンプレッサに連結され且つ第1冷媒回路にも連結され、かくして第1冷媒回路を流れる冷媒と、第3冷媒回路を流れる冷媒との間に熱交換が生じるようにした凝縮器と、第3冷媒回路の冷媒の圧力を低下させる膨張装置と、この膨張器と第2冷媒回路とに連結され、かくして第2冷媒回路を流れる冷媒と、第3冷媒回路を流れる冷媒との間に熱交換が生じるようにした蒸発器と、を含む。冷媒は、加熱及び冷却の両モード下に第3冷媒回路に沿って移動し得ると共に、両モード下での第1、第2、第3の各冷媒回路間移動が防止され得る。
According to the present invention, it is possible to operate under both HP and A / C modes without changing the refrigerant flow direction in the system by doubling the coolant loop and adding a heat exchanger. A cooling system is provided. This cooling system is preferably used for air conditioning in a truck cabin with the engine stopped. In some embodiments, CO 2 is used as a refrigerant in at least one refrigerant circuit.
In one embodiment, the present invention provides a cooling system that includes both a heating mode for heating the cargo compartment and a cooling mode for removing heat from the cargo compartment. The cooling system includes first, second, and third refrigerant circuits, and the first refrigerant circuit includes a first heat exchanger that transfers heat of the refrigerant in the first refrigerant circuit to air, The second refrigerant circuit includes a second heat exchanger that transfers the heat of the air to the second refrigerant circuit. The third refrigerant circuit is connected to the compressor for increasing the pressure of the refrigerant in the third refrigerant circuit, and to the compressor to receive the refrigerant from the compressor, and is also connected to the first refrigerant circuit, and thus the first refrigerant circuit is connected. A condenser in which heat exchange occurs between the flowing refrigerant and the refrigerant flowing in the third refrigerant circuit; an expansion device that reduces the pressure of the refrigerant in the third refrigerant circuit; and the expander and the second refrigerant circuit And an evaporator which is configured to exchange heat between the refrigerant flowing through the second refrigerant circuit and the refrigerant flowing through the third refrigerant circuit. The refrigerant can move along the third refrigerant circuit under both heating and cooling modes, and movement between the first, second, and third refrigerant circuits under both modes can be prevented.

他の実施例において、本発明によれば、荷室を加熱する加熱モードと、荷室を除熱する冷却モードとの何れも備える冷却システムが提供される。本冷却システムには、コンプレッサと、蒸発器と、膨張装置と、凝縮器とを経る第1冷媒回路が含まれ得、この第1冷媒回路に沿って、冷却システムの加熱及び冷却の各モード動作時に冷媒が移動する冷媒流路が画定され得る。本冷却システムには、第1冷媒ポンプを含み且つ凝縮器と熱交換器とを経る第2冷媒回路と、第2冷媒ポンプを含み且つ蒸発器と熱交換器とを経る第3冷媒回路とが更に含まれ得る。第2冷媒ポンプは、加熱モード中に動作され、冷却モード中は停止され得る。   In another embodiment, the present invention provides a cooling system that includes both a heating mode for heating a cargo compartment and a cooling mode for removing heat from the cargo compartment. The cooling system may include a first refrigerant circuit that passes through a compressor, an evaporator, an expansion device, and a condenser, and each mode operation of heating and cooling of the cooling system along the first refrigerant circuit. Sometimes a refrigerant flow path through which the refrigerant moves can be defined. The cooling system includes a second refrigerant circuit including a first refrigerant pump and passing through a condenser and a heat exchanger, and a third refrigerant circuit including a second refrigerant pump and passing through an evaporator and a heat exchanger. Further may be included. The second refrigerant pump can be operated during the heating mode and stopped during the cooling mode.

本発明によれば、冷却システムの運転方法も提供される。本方法には、冷却システムの冷却モード運転時に冷媒をコンプレッサ、蒸発器、膨張装置、凝縮器、の順で冷却回路に沿って送ること、冷却システムの冷却モード運転時に第1ポンプを動作させて熱交換器内で冷媒を循環させ、冷却システムの冷却モード運転時に荷室の熱を冷媒回路内の冷媒に移行させること、が含まれる。本方法には、冷却システムの加熱モード運転時に第1ポンプを停止させること、冷却システムの加熱モード運転時に冷媒を冷却回路に沿って送ること、冷却システムの加熱モード運転時に第2ポンプを作動させて冷媒を熱交換器を通して冷媒回路の冷媒との熱交換関係下に循環させること、冷却システムの加熱モード運転時に冷媒回路内の冷媒の熱を荷室に移行させること、が含まれ得る。   According to the present invention, a method for operating a cooling system is also provided. In this method, the refrigerant is sent along the cooling circuit in the order of the compressor, the evaporator, the expansion device, and the condenser during the cooling mode operation of the cooling system, and the first pump is operated during the cooling mode operation of the cooling system. Circulating the refrigerant in the heat exchanger and transferring the heat of the cargo compartment to the refrigerant in the refrigerant circuit during the cooling mode operation of the cooling system. The method includes stopping the first pump during heating mode operation of the cooling system, sending refrigerant along the cooling circuit during heating mode operation of the cooling system, and operating the second pump during heating mode operation of the cooling system. Circulating the refrigerant through the heat exchanger in a heat exchange relationship with the refrigerant in the refrigerant circuit, and transferring the heat of the refrigerant in the refrigerant circuit to the luggage compartment during the heating mode operation of the cooling system.

本明細書において、“取り付けた”、“連結した”又は“結合した”、“支持された”、“カップリングされた”及びその変形例は、特に断りのない限りその広い意味で用いられ、直接的及び間接的な形態のものを含むものとする。また、“連結した”又は“結合した”及び“カップリングされた”はその物理的又は機械的態様に限定されないものとする。   In this specification, “attached”, “coupled” or “coupled”, “supported”, “coupled” and variations thereof are used in their broader sense unless otherwise specified. Includes direct and indirect forms. Also, “connected” or “coupled” and “coupled” are not limited to their physical or mechanical aspects.

本明細書において、装置又は要素の方向に関する参照(例えば、“中央”、“上方”、“下方”、“前方”、“後方”、その他)は、本発明の説明を簡略化するためのみに使用されるものであって、これに限定しようとするものではない。また、“第1”、“第2”、“第3”とは、説明上使用されるものであって、相対的な重要度又は意義を表示又は付与するものではない。   In this specification, references to device or element orientation (eg, “middle”, “upper”, “lower”, “front”, “rear”, etc.) are intended only to simplify the description of the invention. It is intended to be used and is not intended to be limiting. Further, “first”, “second”, and “third” are used for explanation, and do not indicate or give relative importance or significance.

図1A及び図1Bには、本発明のいくつかの実施例に従う冷却システム10が略示されている。冷却システム10が空調又は冷却(A/C)モードで運転される間、CO2はコンプレッサ12を出た後、図1A及び図1Bの実施例では空冷式ガスクーラー14である第1熱交換器(例えば蒸発器又は凝縮器)に入る。図1Aの実施例では、冷媒流れは3本の実線矢印で示される。1つ以上の運転条件、加熱又は冷却における予測負荷、使用する冷媒のタイプ次第では、コンプレッサ12を出る冷媒は超臨界状態となる。本明細書ではCO2を冷媒として参照するが、他の実施例では、これに限定しないが、水、R12、エンジン冷却材、任意のその他有機系冷媒、R245fa、グリコール、の如きを使用又は代替させることができる。図1Aに示すように、ファン16を、空気流通路開口に隣り合って又は沿って熱交換器14上に位置決めし、冷媒の熱をこのファン16の提供する周囲空気流れに移行させることで、熱交換器14の熱が周囲環境に放熱される。 1A and 1B schematically illustrate a cooling system 10 according to some embodiments of the present invention. While the cooling system 10 is operated in air conditioning or cooling (A / C) mode, the CO 2 exits the compressor 12 and then the first heat exchanger, which is an air-cooled gas cooler 14 in the embodiment of FIGS. 1A and 1B. (E.g. evaporator or condenser) . In the example of FIG. 1A, the refrigerant flow is indicated by three solid arrows. Depending on one or more operating conditions, the expected load in heating or cooling, and the type of refrigerant used, the refrigerant exiting the compressor 12 will be in a supercritical state. Although CO 2 is referred to herein as a refrigerant, in other embodiments, such as, but not limited to, water, R12, engine coolant, any other organic refrigerant, R245fa, glycol, etc. may be used or substituted. Can be made. As shown in FIG. 1A, the fan 16, along adjacently or air flow passage opening is positioned on the heat exchanger 14, by shifting the refrigerant heat to the surrounding air flow provided by the fan 16, The heat of the heat exchanger 14 is radiated to the surrounding environment.

次いで、冷媒は、図1Aの実施例では高温の第2冷却材ループ19により冷却される液冷式ガスクーラー18である第2熱交換器(例えば蒸発器又は凝縮器)に入る。図1Aの実施例では、A/Cモードでのシステム運転中に液体冷却材が第2冷却材ループ19を通して流れ(恐らくは熱交換器14からの冷媒のそれよりも低い質量流量下に)、冷媒温度を一層低下させるが、この熱交換器18の熱負荷は熱交換器14のそれよりも小さくなり得る。他の実施例では、熱交換器18の熱負荷は、熱交換器14及び熱交換器18の相対寸法形状や冷却能力、熱交換器14及び熱交換器18を貫き且つ横断して流れる冷媒及び冷却材の質量流量、熱交換器14用のファン16の有無、熱交換器14及び熱交換器18で使用する冷却材のタイプや冷却能力次第では、熱交換器14が経験する熱負荷と実質的に同等又はそれ以上となる可能性がある。 The refrigerant then enters a second heat exchanger (eg, an evaporator or condenser) , which in the example of FIG. 1A is a liquid cooled gas cooler 18 that is cooled by a hot second coolant loop 19. In the embodiment of FIG. 1A, liquid coolant flows through the second coolant loop 19 (possibly under a lower mass flow rate than that of the refrigerant from the heat exchanger 14) during system operation in A / C mode. Although the temperature is further reduced, the heat load of this heat exchanger 18 can be smaller than that of the heat exchanger 14. In another embodiment, the heat load of the heat exchanger 18, the refrigerant flows relative dimensions and cooling capacity of the heat exchanger 14 and heat exchanger 18, heat exchanger 14 and heat exchanger 18 to penetrate and traverse and mass flow rate of the coolant, whether fan 16 of heat exchanger 14, depending on the type or cooling capacity of the coolant used in heat exchanger 14 and heat exchanger 18, the heat load substantially heat exchanger 14 experiences May be equivalent or better.

図1Aに示すように、熱交換器18を出た冷媒は膨張装置または膨張弁22に向かう前に更に冷却されるべく、吸引ライン内熱交換器(SLHX)20(以下、熱交換器20とも称する)の高圧側に流入し得る。膨張装置または膨張弁22を出た冷媒は空気対冷媒式蒸発器24に流入し得る。空気流通路開口に隣り合って又は沿って空気対冷媒式蒸発器24上にファン(図示せず)を位置決めし得る。ある実施例では、冷却需要度が低い間はファンを停止させる及び又は冷却システム10の電力消費量を制限して効率を改善する。ファンを停止する又は減速動作させる実施例では、蒸発器24の熱負荷は、熱交換器20から冷媒を受ける液体対冷媒式蒸発器26のそれよりも遙かに小さい値に制限され得る。 As shown in FIG. 1A, the refrigerant leaving the heat exchanger 18 is further cooled before going to the expansion device or expansion valve 22, so that the heat exchanger (SLHX) 20 in the suction line (hereinafter also referred to as the heat exchanger 20). May flow into the high pressure side. The refrigerant exiting the expansion device or expansion valve 22 can flow into the air-to-refrigerant evaporator 24. A fan (not shown) may be positioned on the air to refrigerant evaporator 24 next to or along the airflow passage opening. In some embodiments, the fan is stopped while the cooling demand is low and / or the power consumption of the cooling system 10 is limited to improve efficiency. In the embodiment to or deceleration stops the fan, the heat load of the steam Hatsuki 24, than that of the liquid-refrigerant evaporator 26 for receiving the refrigerant from the heat exchanger 20 may be limited to a small value much.

液体対冷媒式蒸発器26の場合、冷媒は蒸発し、別の、低温の第2冷却材ループ28(以下、低温冷却材ループ28とも称する)を出てこの液体対冷媒式蒸発器26を通過して流れる冷却材(例えば、グリコール、水、R12、エンジン冷却材、任意の有機系冷媒、R245fa、空気、その他)から熱エネルギーを奪ってこの冷却材を冷却する。空気対冷媒式蒸発器24は液体対冷媒式蒸発器26の上流側又は下流側の何れかに配置可能である。この点は熱交換器14に関する熱交換器18の配置についても言えるが、A/Cモード下に冷却システム10を運転する間は、熱交換器18内で液体の速度低下又は停滞が生じることによる過剰加熱及び又は沸騰を回避することが望ましい。 In the case of the liquid-to-refrigerant evaporator 26, the refrigerant evaporates and passes through the liquid-to-refrigerant evaporator 26 through another low-temperature second coolant loop 28 (hereinafter also referred to as the low-temperature coolant loop 28). Then, heat energy is taken away from the flowing coolant (eg, glycol, water, R12, engine coolant, any organic refrigerant, R245fa, air, etc.) to cool the coolant. The air-to-refrigerant evaporator 24 can be located either upstream or downstream of the liquid-to-refrigerant evaporator 26. Although true for the arrangement of the heat exchanger 18 this regarding heat exchanger 14, while operating the cooling system 10 under A / C mode is by slowing or stagnation of the liquid in the heat exchanger 18 occurs It is desirable to avoid overheating and / or boiling.

液体対冷媒式蒸発器26を出た冷媒は吸引ライン内熱交換器20内の高圧の冷媒に熱を放出し得る。吸引ライン内熱交換器20の上流側の低圧側にアキュムレータ(図1A〜図2Bには図示せず)を位置決めし得る。アキュムレータは別ユニットとし、又は吸引ライン内熱交換器20に一体的に直結され得る。
低温冷却材ループ28は、液体対冷媒式蒸発器26の他に、この液体対冷媒式蒸発器26の液体側を通して冷却液を移動させるための低温ポンプ29を含み得る。冷却材の熱が液体対冷媒式蒸発器26内で冷媒に移行される間、内部空間又は車室32,例えばトラック又はその他自動車の車室のような空間に取り付け得る熱交換器冷却コア30が、低温冷却材ループ28からの熱を放散させるべく動作され得る。熱交換器冷却コア30には、車室32内の空気を冷却し及び又は車室32の空気を除湿し得るファン又はブロワのような空気動作装置34が付設され得る。ある実施例では、熱交換器冷却コア30を通る又は横断する空気流れが露点以下に冷却されると、第2冷却材ループ19を通して少量の冷却液が循環して車室(3本の点線矢印で示す)に流入する空気が再加熱される。
The refrigerant leaving the liquid-to-refrigerant evaporator 26 can release heat to the high-pressure refrigerant in the suction line heat exchanger 20. An accumulator (not shown in FIGS. 1A to 2B) may be positioned on the low pressure side upstream of the heat exchanger 20 in the suction line. The accumulator can be a separate unit or can be directly connected to the heat exchanger 20 in the suction line.
In addition to the liquid-to-refrigerant evaporator 26, the cryogenic coolant loop 28 may include a cryogenic pump 29 for moving coolant through the liquid side of the liquid-to-refrigerant evaporator 26. While the heat of the coolant is transferred to the refrigerant in the liquid-to-refrigerant evaporator 26, there is a heat exchanger cooling core 30 that can be attached to the interior space or space 32 such as a truck or other automobile compartment. May be operated to dissipate heat from the cryogenic coolant loop 28. The heat exchanger cooling core 30 may be provided with an air operating device 34 such as a fan or blower that can cool the air in the passenger compartment 32 and / or dehumidify the air in the passenger compartment 32. In one embodiment, when the air flow through or across the heat exchanger cooling core 30 is cooled below the dew point, a small amount of coolant circulates through the second coolant loop 19 to cause a passenger compartment (three dotted arrows). The air flowing in) is reheated.

図1Bには加熱(HP)モード運転時の冷却システム10を例示する。3つの実線矢印で示すように、冷媒はA/Cモード運転に関して先に説明したと同じ方向で冷却システム10内を流動するが、熱交換器14に隣り合うファン16は停止され、高温の冷却液をポンプ35により高温冷却材ループ19を通してポンプ送りして熱交換器18内の冷媒を冷却する。
低温冷却材ループ28内の低温ポンプ29を停止させ、空気対冷媒ファン34を動作させ得る。これにより、高温の冷却材の熱を空気対冷却材熱交換器のヒーターコア36内の空気流れに移行させて車室32の内部を一層加熱することが可能になる。低温時にHPモードで冷却システム10を運転する際の性能係数(COP)を向上させるため、廃熱源42、例えば補助電源ユニット44用の冷却システム43の如きからの廃熱空気流れ40を空気対冷媒式蒸発器24を通して送ることができる。
他の実施例では、廃熱源及び又は別の廃熱源42も同様に又は代替的に、液体対液体熱交換器蒸発器又は、一体的に積層した補助電源ユニット(APU)用クーラー及び蒸発器冷却材のループに熱を提供し得る。後者の場合、廃熱源42を利用することで余分な空熱式蒸発器が無用化され、“クーラー”コアが、空間内の空気の追加熱源となり得る。
FIG. 1B illustrates the cooling system 10 during heating (HP) mode operation. As indicated by the three solid arrows, the refrigerant flows in the cooling system 10 in the same direction as previously described for A / C mode operation, but the fan 16 adjacent to the heat exchanger 14 is stopped and the high temperature cooling is performed. The liquid is pumped through the high temperature coolant loop 19 by the pump 35 to cool the refrigerant in the heat exchanger 18.
The cold pump 29 in the cold coolant loop 28 may be stopped and the air-to-refrigerant fan 34 may be operated. As a result, the heat of the high-temperature coolant can be transferred to the air flow in the heater core 36 of the air-to-coolant heat exchanger to further heat the interior of the passenger compartment 32. In order to improve the coefficient of performance (COP) when operating the cooling system 10 in the HP mode at low temperatures, the waste heat air stream 40 from the waste heat source 42, such as the cooling system 43 for the auxiliary power unit 44, is air to refrigerant. It can be sent through the evaporator 24.
In other embodiments, the waste heat source and / or another waste heat source 42 may, or alternatively, be a liquid-to-liquid heat exchanger evaporator or integrally stacked auxiliary power supply unit (APU) cooler and evaporator cooling. Heat may be provided to the material loop. In the latter case, utilizing the waste heat source 42 eliminates the need for an extra air-heated evaporator, and the “cooler” core can be an additional heat source for air in the space.

図2A及び図2Bには本発明に従う冷却システム10の別態様の実施例が例示される。
図2A及び図2Bに示す冷却システムは図1A及び図1Bに例示した先に説明した実施例と多くの点で類似しているため、両実施例間で一致しない機能構造部分及び要素を除き、図2A及び図2Bの実施例の機能構造部分及び要素の詳しい説明(及びその代替物)については図1A及び図1Bの実施例に関する先の説明が参照される。
図2Aには冷却システム10が簡略化して例示されている。本実施例の冷却システム10では、低温冷却材ループ28と、高温冷却材ループ19と、APU冷却材システム43の冷却材ライン46とが相互に直接的にポンプ送りされ、各ループ19及び28で必要なのは液体ポンプ47(APU冷却材ループポンプは含まない)のみである。
2A and 2B illustrate another embodiment of a cooling system 10 according to the present invention.
The cooling system shown in FIGS. 2A and 2B is similar in many respects to the previously described embodiment illustrated in FIGS. 1A and 1B, except for functional structural parts and elements that do not match between the two embodiments. For a detailed description (and alternatives) of the functional structure portions and elements of the embodiment of FIGS. 2A and 2B, reference is made to the previous description of the embodiment of FIGS. 1A and 1B.
FIG. 2A illustrates a simplified cooling system 10. In the cooling system 10 of this embodiment, the low temperature coolant loop 28, the high temperature coolant loop 19, and the coolant line 46 of the APU coolant system 43 are directly pumped to each other, All that is required is a liquid pump 47 (not including the APU coolant loop pump).

図2Aに示すように、液体弁50、52、54、56、58、59からなる弁マトリクス48を使用して、HP及びA/Cの各モード下に冷却材流れを所望位置に送ることができる。これにより、空気対冷媒式蒸発器24が無用化され得、クーラーコア30及びヒーターコア36の機能を、ヒーター/クーラーコア60の形の熱交換器としてまとめることが可能となる。   As shown in FIG. 2A, a valve matrix 48 consisting of liquid valves 50, 52, 54, 56, 58, 59 is used to direct the coolant flow to the desired location under the HP and A / C modes. it can. Thereby, the air-to-refrigerant evaporator 24 can be made useless, and the functions of the cooler core 30 and the heater core 36 can be integrated as a heat exchanger in the form of a heater / cooler core 60.

例えば、A/Cモード運転時に弁59(点線で示す)を開放し、弁56及び58(実線で示す)を閉じ、弁52、54を開放し、弁50を閉じると、APU冷却材は低温冷却材ループ28(液体対冷媒式蒸発器26を加熱する)には流入せず、従って冷却材は高温ループ19からは熱交換器18に入らず、他方、低温冷却材ループ28内の冷却材の熱が液体対冷媒式蒸発器26内の冷媒に放熱され、この冷却材が、ヒーター/クーラーコア60を通過する空気流れから熱を受ける。用途によっては、冷媒温度が周囲温度よりも低くなってシステムのCOPが向上することから、少量の冷却液を弁50と熱交換器18に通した方が良い場合がある。
図2Bに示すように、HPモード運転時には弁59(実線で示す)を閉じ又は調整し、弁56及び58(点線で示す)を開放し、弁52及び54を閉じ、弁50を開放するとAPU冷却材が液体対冷媒式蒸発器26に送られ、次いで、ヒーター/クーラーコア60を通らずにAPU44に直接循環され、他方、高温ループ19内の冷却材は熱交換器18を通して循環されて冷媒の熱を受け、次いでこの熱をヒーター/クーラーコア60を通過する空気流れに放出する。
For example, when A / C mode operation is performed, valve 59 (shown in dotted line) is opened, valves 56 and 58 (shown in solid line) are closed, valves 52 and 54 are opened, and valve 50 is closed. The coolant does not flow into the coolant loop 28 (which heats the liquid-to-refrigerant evaporator 26), so the coolant does not enter the heat exchanger 18 from the high temperature loop 19, while the coolant in the low temperature coolant loop 28. This heat is dissipated to the refrigerant in the liquid-to-refrigerant evaporator 26, and this coolant receives heat from the air flow passing through the heater / cooler core 60. Depending on the application, it may be better to pass a small amount of coolant through the valve 50 and the heat exchanger 18 because the refrigerant temperature will be lower than the ambient temperature and the COP of the system will improve.
As shown in FIG. 2B, during HP mode operation, valve 59 (shown in solid line) is closed or adjusted, valves 56 and 58 (shown in dotted line) are opened, valves 52 and 54 are closed, and valve 50 is opened. The coolant is sent to the liquid-to-refrigerant evaporator 26 and then circulated directly to the APU 44 without passing through the heater / cooler core 60, while the coolant in the hot loop 19 is circulated through the heat exchanger 18 to refrigerate. The heat is then released into the air stream passing through the heater / cooler core 60.

図3A及び図3Bには、本発明に従う冷却システム10の別態様の実施例を例示する。図3A及び図3Bに示す冷却システムは、先に図1A〜図2Bに例示した実施例と多くの点で類似するため、両実施例間で一致しない機能構造部分及び要素を除き、図3A及び図3Bの実施例の機能構造部分及び要素の詳しい説明(及びその代替構成)については図1A〜図2Bの各実施例に関する先の説明が参照される。
図3A及び図3Bの冷却システム10は、空気対冷媒式蒸発器24が除去され空熱式冷却材熱交換器66で代替されている点が図1A及び1Bに示す実施例と異なっている。空熱式冷却材熱交換器66は、低温冷却材ループ28内でバイパスライン68に追加され、3方弁70(又は一連の2方弁)により、クーラーコア30及び空熱式冷却材熱交換器66を通過する冷却材流れを制御する。
3A and 3B illustrate an alternative embodiment of the cooling system 10 according to the present invention. The cooling system shown in FIGS. 3A and 3B is similar in many respects to the embodiment illustrated above in FIGS. 1A-2B, and therefore, with the exception of functional structural portions and elements that do not match between the embodiments. For a detailed description (and alternative configurations) of the functional structure portions and elements of the embodiment of FIG. 3B, reference is made to the previous description of each embodiment of FIGS. 1A-2B.
The cooling system 10 of FIGS. 3A and 3B differs from the embodiment shown in FIGS. 1A and 1B in that the air-to-refrigerant evaporator 24 is removed and replaced with an air-heated coolant heat exchanger 66. An air-heated coolant heat exchanger 66 is added to the bypass line 68 within the low-temperature coolant loop 28, and a three-way valve 70 (or a series of two-way valves) causes the cooler core 30 and air-heated coolant heat exchange. Control the coolant flow through the vessel 66.

図3Aに示すように、A/Cモード運転時には弁70が空熱式冷却材熱交換器66ではなくむしろクーラーコア30を通して冷却材を送り、かくして、低温冷却材ループ28内を流動する冷却材が、クーラーコア30を通過する空気流れの熱を吸収し得る。高温ループの動作は図1A及び図1Bに示す冷却システム10におけるそれと実質的に類似し得るものである。空熱式冷却材熱交換器66は、例えば、ゼネレータからの液体廃熱流れのようなその他の熱源を利用するその他の任意タイプの熱交換器で代替させることが可能である。
図3Bに示すように、HPモード運転時には弁70が、クーラーコア30を通してではなくむしろ空熱式冷却材熱交換器66を通して冷却材を送り、かくして、空熱式冷却材熱交換器66を通る周囲空気の熱が低温冷却材ループ28内を流れる冷却材に移行される。
As shown in FIG. 3A, during A / C mode operation, the valve 70 sends coolant through the cooler core 30 rather than through the air-heated coolant heat exchanger 66, and thus the coolant flowing in the low temperature coolant loop 28. However, the heat of the air flow passing through the cooler core 30 can be absorbed. The operation of the hot loop can be substantially similar to that in the cooling system 10 shown in FIGS. 1A and 1B. The air-heated coolant heat exchanger 66 can be replaced with any other type of heat exchanger that utilizes other heat sources, such as, for example, a liquid waste heat stream from a generator.
As shown in FIG. 3B, during HP mode operation, the valve 70 sends coolant through the air-cooled coolant heat exchanger 66 rather than through the cooler core 30 and thus passes through the air-heated coolant heat exchanger 66. The heat of the ambient air is transferred to the coolant flowing in the low temperature coolant loop 28.

図4A及び図4Bには、本発明に従う冷却システム10の別態様の実施例が例示される。図4A及び図4Bに示す冷却システムは先に図1A〜図3Bに例示した実施例と多くの点で類似するものであるので、両実施例間で一致しない機能構造部分及び要素を除き、図4A及び図4Bの実施例の機能構造部分及び要素の詳しい説明(及びその代替構成)については図1A〜図3Bの各実施例に関する先の説明が参照される。
図4A及び図4Bに示すように、本実施例の冷却システム10は、熱交換器14及び空気対冷媒式蒸発器24が何れも除去され、クーラーコア30及びヒーターコア36の機能が図2A及び図2Bに関連して議論したようなヒーター/クーラーコア60としてまとめられ、図3A及び図3Bに関連した議論したような空熱式冷却材熱交換器66が高温ループ19及び低温冷却材ループ28の両方の内部に配管され、高温ループ19内に設けた3方弁74(又は一連の2方弁)と、低温冷却材ループ28内に設けた3方弁78が、高温ループ19内の熱交換器60及び低温冷却材ループ28内の空熱式冷却材熱交換器66を夫々流れる冷却材流れを制御する点で、図1A及び図1Bに示す冷却システム10とは異なる。
図4Aに示すように、A/Cモード運転時には弁78により、低温ループ19内の冷却材を空熱式冷却材熱交換器66ではなくむしろ熱交換器であるヒーター/クーラーコア60を通して送ることで車室32を除熱し、弁74により、冷却材をヒーター/クーラーコア60ではなくむしろ空熱式冷却材熱交換器66を通して高温ループ19から送ることで、熱交換器18からの冷却材によって吸収した熱を空熱式冷却材熱交換器66を通して周囲空気流れに放出させる。
図4Bに示すように、HPモード運転時には、高温ループ19内の冷却材は弁74によって空熱式冷却材熱交換器66を通してではなくむしろヒーター/クーラーコア60を通して送られ、他方、低温冷却材ループ28内の冷却材は、弁78によって、ヒーター/クーラーコア60ではなくむしろ空熱式冷却材熱交換器66を通して送られ、かくして熱交換器68を通して流動する周囲空気流れから熱を吸収する。
以上、本発明を実施例を参照して説明したが、本発明の内で種々の変更をなし得ることを理解されたい。
4A and 4B illustrate another embodiment of a cooling system 10 according to the present invention. The cooling system shown in FIGS. 4A and 4B is similar in many respects to the embodiment illustrated above in FIGS. 1A-3B, except for the functional structural parts and elements that do not match between the two embodiments. For a detailed description (and alternative configurations) of the functional structure portions and elements of the embodiment of 4A and 4B, reference is made to the previous description of each embodiment of FIGS. 1A-3B.
As shown in FIG. 4A and FIG. 4B, the cooling system 10 of this embodiment has both the heat exchanger 14 and the air-to-refrigerant evaporator 24 removed, and the functions of the cooler core 30 and the heater core 36 are as shown in FIG. An air-heated coolant heat exchanger 66, as discussed in connection with FIGS. 3A and 3B, is summarized as a heater / cooler core 60 as discussed in connection with FIG. The three-way valve 74 (or a series of two-way valves) provided in the high-temperature loop 19 and the three-way valve 78 provided in the low-temperature coolant loop 28 are connected to the heat in the high-temperature loop 19. It differs from the cooling system 10 shown in FIGS. 1A and 1B in that the coolant flow through the exchanger 60 and the air-cooled coolant heat exchanger 66 in the low temperature coolant loop 28 is controlled.
As shown in FIG. 4A, during the A / C mode operation, the valve 78 causes the coolant in the low temperature loop 19 to be sent through the heater / cooler core 60 which is a heat exchanger rather than the air-heated coolant heat exchanger 66. The vehicle compartment 32 is removed by heat and the valve 74 causes the coolant to flow from the hot loop 19 through the air-cooled coolant heat exchanger 66 rather than through the heater / cooler core 60, so that the coolant from the heat exchanger 18 The absorbed heat is released through the air-heated coolant heat exchanger 66 into the ambient air stream.
As shown in FIG. 4B, during HP mode operation, the coolant in the high temperature loop 19 is routed by the valve 74 through the heater / cooler core 60 rather than through the air-heated coolant heat exchanger 66, while the low temperature coolant. The coolant in the loop 28 is sent by the valve 78 through the air-cooled coolant heat exchanger 66 rather than the heater / cooler core 60, thus absorbing heat from the ambient air stream flowing through the heat exchanger 68.
Although the present invention has been described with reference to the embodiments, it should be understood that various modifications can be made within the present invention.

本発明の実施例に従う冷却システムの、冷却モード運転時における概略図である。It is the schematic at the time of cooling mode operation | movement of the cooling system according to the Example of this invention. 図1Aの冷却システムの、加熱モード運転時における概略図である。It is the schematic at the time of heating mode operation | movement of the cooling system of FIG. 1A. 本発明の他の実施例に従う冷却システムの、冷却モード運転時における概略図である。FIG. 6 is a schematic diagram of a cooling system according to another embodiment of the present invention during cooling mode operation. 図2Aの冷却システムの、加熱モード運転時における概略図である。It is the schematic at the time of heating mode operation | movement of the cooling system of FIG. 2A. 本発明の他の実施例に従う冷却システムの、冷却モード運転時における概略図である。FIG. 6 is a schematic diagram of a cooling system according to another embodiment of the present invention during cooling mode operation. 図3Aの冷却システムの、加熱モード運転時における概略図である。It is the schematic at the time of heating mode operation | movement of the cooling system of FIG. 3A. 本発明の他の実施例に従う冷却システムの、冷却モード運転時における概略図である。FIG. 6 is a schematic diagram of a cooling system according to another embodiment of the present invention during cooling mode operation. 図4Aの冷却システムの、加熱モード運転時における概略図である。It is the schematic at the time of heating mode operation | movement of the cooling system of FIG. 4A.

符号の説明Explanation of symbols

10 冷却システム
12 コンプレッサ
14 第1熱交換器
16 ファン
18 第2熱交換器
19 高温冷却材ループ
20 吸引ライン内熱交換器
22 膨張弁
24 空気対冷媒式蒸発器
26 液体対冷媒式蒸発器
28 第2冷却材ループ
29 低温ポンプ
30 熱交換器冷却コア
32 車室
34 空気対冷媒ファン
35 ポンプ
36 ヒーターコア
40 廃熱空気流れ
42 廃熱源
43 APU冷却材システム
44 補助電源ユニット
46 冷却材ライン
48 弁マトリクス
50、52、54、56、58、59 液体弁
60 ヒーター/クーラーコア
66 空熱式冷却材熱交換器
68 バイパスライン
70、78 3方弁
DESCRIPTION OF SYMBOLS 10 Cooling system 12 Compressor 14 1st heat exchanger 16 Fan 18 2nd heat exchanger 19 High temperature coolant loop 20 Heat exchanger in suction line 22 Expansion valve 24 Air-to-refrigerant evaporator 26 Liquid-to-refrigerant evaporator 28 2 Coolant loop 29 Low temperature pump 30 Heat exchanger cooling core 32 Car compartment 34 Air-to-refrigerant fan 35 Pump 36 Heater core 40 Waste heat air flow 42 Waste heat source 43 APU coolant system 44 Auxiliary power supply unit 46 Coolant line 48 Valve matrix 50, 52, 54, 56, 58, 59 Liquid valve 60 Heater / cooler core 66 Air-heated coolant heat exchanger 68 Bypass line 70, 78 Three-way valve

Claims (23)

荷室に熱を提供する加熱モード及び荷室を除熱する冷却モードの何れをも有する冷却システムであって、
第1冷媒回路の冷媒の熱を空気に移行させるための第1熱交換器を含む第1冷媒回路と、
第2冷媒回路にして、空気の熱を該第2冷媒回路に移行させるための第2熱交換器を含む第2冷媒回路と、
第3冷媒回路にして、該第3冷媒回路の冷媒の圧力を増大するコンプレッサと、該コンプレッサに連結されて該コンプレッサの熱を受け、第1冷媒回路を通して移動する冷媒と、第3冷媒回路を通して移動する冷媒との間に熱交換が生じ得るように第1冷媒回路に連結した凝縮器と、第3冷媒回路の冷媒の圧力を減少させる膨張装置と、該膨張装置に連結され、第2冷媒回路を通して移動する冷媒と、第3冷媒回路を通して移動する冷媒との間に熱交換が生じるように第2冷媒回路に連結した蒸発器とを含み、加熱及び冷却の両運転モード時に冷媒が該第3冷媒回路内を共通方向に沿って移動する第3冷媒回路と、
を含み、
加熱及び冷却の両運転モード時の、第1冷媒回路、第2冷媒回路、第3冷媒回路の各間での冷媒移動が防止される冷却システム。
A cooling system having both a heating mode for providing heat to the cargo compartment and a cooling mode for removing heat from the cargo compartment,
A first refrigerant circuit including a first heat exchanger for transferring heat of refrigerant in the first refrigerant circuit to air;
A second refrigerant circuit including a second heat exchanger for transferring the heat of air to the second refrigerant circuit as a second refrigerant circuit;
A third refrigerant circuit, a compressor that increases the pressure of the refrigerant in the third refrigerant circuit, a refrigerant that is connected to the compressor and receives heat of the compressor and moves through the first refrigerant circuit, and a third refrigerant circuit A condenser connected to the first refrigerant circuit so that heat exchange can occur with the moving refrigerant, an expansion device for reducing the pressure of the refrigerant in the third refrigerant circuit, and a second refrigerant connected to the expansion device An evaporator connected to the second refrigerant circuit so that heat exchange occurs between the refrigerant moving through the circuit and the refrigerant moving through the third refrigerant circuit, and the refrigerant is in the first and second operating modes. A third refrigerant circuit moving along a common direction in the three refrigerant circuit;
Including
A cooling system that prevents refrigerant from moving between the first refrigerant circuit, the second refrigerant circuit, and the third refrigerant circuit in both heating and cooling operation modes.
凝縮器が液冷式ガスクーラである請求項1の冷却システム。 The cooling system of claim 1, wherein the condenser is a liquid-cooled gas cooler. 液冷式ガスクーラーに直列に連結され且つコンプレッサ及び膨張装置の少なくとも一方に連結した空冷式ガスクーラーを更に含む請求項2の冷却システム。 The cooling system according to claim 2, further comprising an air-cooled gas cooler connected in series to the liquid-cooled gas cooler and connected to at least one of the compressor and the expansion device. 蒸発器が液体加熱式の蒸発器である請求項1の冷却システム。 2. The cooling system according to claim 1, wherein the evaporator is a liquid heating type evaporator. 液体加熱式の蒸発器と直列に連結され且つ膨張装置及びコンプレッサの少なくとも一方に連結した空気加熱式の蒸発器を更に含む請求項4の冷却システム。 5. The cooling system of claim 4, further comprising an air heated evaporator connected in series with the liquid heated evaporator and connected to at least one of the expansion device and the compressor. 第3冷媒回路内で凝縮器、膨張弁、蒸発器、コンプレッサに連結した吸引ライン熱交換器を更に含む請求項1の冷却システム。 The cooling system of claim 1, further comprising a suction line heat exchanger connected to the condenser, expansion valve, evaporator, and compressor in the third refrigerant circuit. 第3冷媒回路の冷媒が二酸化炭素である請求項1の冷却システム。 The cooling system according to claim 1, wherein the refrigerant in the third refrigerant circuit is carbon dioxide. 第1熱交換器と第2熱交換器とを単一の熱交換器としてまとめた請求項1の冷却システム。 The cooling system of Claim 1 which put together the 1st heat exchanger and the 2nd heat exchanger as a single heat exchanger. 加熱モード運転時に冷却システムに熱を提供するための、第1冷媒回路、第2冷媒回路、第3冷媒回路とは別個の熱源を更に含む請求項1の冷却システム。 The cooling system of claim 1, further comprising a heat source separate from the first refrigerant circuit, the second refrigerant circuit, and the third refrigerant circuit for providing heat to the cooling system during heating mode operation. 荷室を加熱するための加熱モードと、荷室を除熱するための冷却モードとを何れも有する冷却システムであって、
コンプレッサ、蒸発器、膨張装置、凝縮器、を経る第1冷媒回路にして、冷却システムの加熱モード及び冷却モードの各運転時に冷媒を第1冷媒回路に沿った方向で移動させるための流路を画定する第1冷媒回路と、
第1冷媒ポンプを含み、凝縮器と、熱交換器とを経る第2冷媒回路と、
第2冷媒ポンプを含み、蒸発器と、熱交換器とを経る第3冷媒回路とを含み、
前記第2冷媒ポンプが冷却システムの加熱モード運転時に動作され、冷却システムの冷却モード運転時は停止される、
冷却システム。
A cooling system having both a heating mode for heating the cargo compartment and a cooling mode for removing heat from the cargo compartment,
The first refrigerant circuit that passes through the compressor, the evaporator, the expansion device, and the condenser has a flow path for moving the refrigerant in the direction along the first refrigerant circuit during each operation in the heating mode and the cooling mode of the cooling system. A first refrigerant circuit defining;
A second refrigerant circuit including a first refrigerant pump and passing through a condenser and a heat exchanger;
Including a second refrigerant pump, including an evaporator and a third refrigerant circuit passing through the heat exchanger;
The second refrigerant pump is operated during the heating mode operation of the cooling system, and is stopped during the cooling mode operation of the cooling system;
Cooling system.
第2冷媒回路が第1冷媒回路から離間され、かくして、第1冷媒回路及び第2冷媒回路間での冷媒の移動が防止され、第2冷媒回路が凝縮器を貫いて伸延され、かくして、第1冷媒回路を通して移動する冷媒と、第2冷媒回路を通して移動する冷媒との間に熱交換が生じる請求項10の冷却システム。 The second refrigerant circuit is spaced from the first refrigerant circuit, thus preventing movement of the refrigerant between the first refrigerant circuit and the second refrigerant circuit, and the second refrigerant circuit is extended through the condenser, thus the first refrigerant circuit. The cooling system according to claim 10, wherein heat exchange occurs between the refrigerant moving through the first refrigerant circuit and the refrigerant moving through the second refrigerant circuit. 第3冷媒回路が第1冷媒回路から離間され、かくして、第1冷媒回路及び第3冷媒回路間での冷媒移動が防止され、第3冷媒回路が蒸発器を貫いて伸延され、かくして、第1冷媒回路を通して移動する冷媒と、第3冷媒回路を通して移動する冷媒との間に熱交換が生じる請求項10の冷却システム。 The third refrigerant circuit is spaced from the first refrigerant circuit, thus preventing refrigerant movement between the first refrigerant circuit and the third refrigerant circuit, and the third refrigerant circuit is extended through the evaporator, thus the first refrigerant circuit. The cooling system according to claim 10, wherein heat exchange occurs between the refrigerant moving through the refrigerant circuit and the refrigerant moving through the third refrigerant circuit. 第1冷媒回路が吸引ライン熱交換器を含む請求項10の冷却システム。 The cooling system of claim 10, wherein the first refrigerant circuit includes a suction line heat exchanger. 熱交換器が、第1熱交換器コア及び第2熱交換器コアを含み、第1熱交換器コアが第2冷媒回路と関連し、第2熱交換器コアが第3冷媒回路と関連する請求項10の冷却システム。 The heat exchanger includes a first heat exchanger core and a second heat exchanger core, the first heat exchanger core is associated with the second refrigerant circuit, and the second heat exchanger core is associated with the third refrigerant circuit. The cooling system of claim 10. 冷却システムの加熱モード運転時に冷却システムに熱を提供するための、第1冷媒回路、第2冷媒回路、第3冷媒回路、とは別個の熱源を更に含む請求項10の冷却システム。 The cooling system of claim 10, further comprising a heat source separate from the first refrigerant circuit, the second refrigerant circuit, and the third refrigerant circuit for providing heat to the cooling system during heating mode operation of the cooling system. 蒸発器が液体加熱式蒸発器であり、凝縮器が液冷式ガスクーラーである請求項10の冷却システム。 The cooling system according to claim 10, wherein the evaporator is a liquid heating evaporator and the condenser is a liquid-cooled gas cooler. 液冷式ガスクーラーと直列に連結した空冷式ガスクーラーを更に含む請求項16の冷却システム。 The cooling system of claim 16, further comprising an air-cooled gas cooler connected in series with the liquid-cooled gas cooler. 液体加熱式蒸発器と直列に連結した空気加熱式蒸発器を更に含む請求項16の冷却システム。 The cooling system of claim 16, further comprising an air heated evaporator connected in series with the liquid heated evaporator. 冷却システムの運転方法であって、
冷却システムの冷却モード運転時に、冷媒をコンプレッサ、蒸発器、膨張装置、凝縮器を経る方向で冷媒回路に沿って送ること、
冷却システムの冷却モード運転時に第1ポンプを作動させて熱交換器を通して冷媒を循環させること、
冷却システムの冷却モード運転時に荷室の熱を冷媒回路内の冷媒に移行させること、
冷却システムの加熱運転モード時に第1ポンプを停止すること、
冷却システムの加熱運転モード時に冷媒回路に沿った方向で冷媒を送ること、
冷媒回路の加熱運転モード時に第2ポンプを作動させて熱交換器を通して冷媒回路の冷媒と熱交換関係下に冷媒を循環させること、
冷却システムの加熱運転モード時に冷媒回路内の冷媒の熱を荷室に移行させること、
を含む方法。
A method of operating a cooling system,
Sending the refrigerant along the refrigerant circuit in the direction through the compressor, evaporator, expansion device, condenser during cooling mode operation of the cooling system;
Circulating the refrigerant through the heat exchanger by operating the first pump during the cooling mode operation of the cooling system;
Transferring the heat of the luggage compartment to the refrigerant in the refrigerant circuit during the cooling mode operation of the cooling system;
Stopping the first pump during the heating operation mode of the cooling system;
Sending the refrigerant in the direction along the refrigerant circuit during the heating operation mode of the cooling system,
Circulating the refrigerant in a heat exchange relationship with the refrigerant in the refrigerant circuit through the heat exchanger by operating the second pump during the heating operation mode of the refrigerant circuit;
Transferring the heat of the refrigerant in the refrigerant circuit to the cargo compartment during the heating operation mode of the cooling system;
Including methods.
冷却システムの加熱運転モード時に、冷媒回路とは別個の熱源により冷媒を加熱することを更に含む請求項19の方法。 20. The method of claim 19, further comprising heating the refrigerant with a heat source separate from the refrigerant circuit during the heating mode of operation of the cooling system. 冷媒回路に沿って設けた吸引ライン熱交換器を使用して冷媒を冷却することを更に含む請求項19の方法。 20. The method of claim 19, further comprising cooling the refrigerant using a suction line heat exchanger provided along the refrigerant circuit. 冷却システムの冷却運転モード時に、空気加熱式蒸発器及び液体加熱式蒸発器を使用して冷媒を加熱することを更に含む請求項19の方法。 20. The method of claim 19, further comprising heating the refrigerant using an air heated evaporator and a liquid heated evaporator during a cooling mode of operation of the cooling system. 冷却システムの加熱運転モード時に、空冷式凝縮器及び液冷式凝縮器を使用して冷媒を冷却することを更に含む請求項19の方法。 20. The method of claim 19, further comprising cooling the refrigerant using an air cooled condenser and a liquid cooled condenser during the heating mode of operation of the cooling system.
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