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WO2008056594A1 - Refrigeration system - Google Patents

Refrigeration system Download PDF

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Publication number
WO2008056594A1
WO2008056594A1 PCT/JP2007/071295 JP2007071295W WO2008056594A1 WO 2008056594 A1 WO2008056594 A1 WO 2008056594A1 JP 2007071295 W JP2007071295 W JP 2007071295W WO 2008056594 A1 WO2008056594 A1 WO 2008056594A1
Authority
WO
WIPO (PCT)
Prior art keywords
refrigeration system
thermal siphon
liquid
compressor
temperature
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/JP2007/071295
Other languages
French (fr)
Japanese (ja)
Inventor
Jiro Iizuka
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.)
Sanden Corp
Original Assignee
Sanden Corp
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 Sanden Corp filed Critical Sanden Corp
Publication of WO2008056594A1 publication Critical patent/WO2008056594A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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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
    • F25B31/00Compressor arrangements
    • F25B31/006Cooling of compressor or motor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C18/00Rotary-piston pumps specially adapted for elastic fluids
    • F04C18/02Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents
    • F04C18/0207Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form
    • F04C18/0215Rotary-piston pumps specially adapted for elastic fluids of arcuate-engagement type, i.e. with circular translatory movement of co-operating members, each member having the same number of teeth or tooth-equivalents both members having co-operating elements in spiral form where only one member is moving
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C23/00Combinations of two or more pumps, each being of rotary-piston or oscillating-piston type, specially adapted for elastic fluids; Pumping installations specially adapted for elastic fluids; Multi-stage pumps specially adapted for elastic fluids
    • F04C23/008Hermetic pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C29/00Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
    • F04C29/04Heating; Cooling; Heat insulation
    • F04C29/045Heating; Cooling; Heat insulation of the electric motor in hermetic pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D15/00Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
    • F28D15/02Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
    • F28D15/0266Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C2240/00Components
    • F04C2240/30Casings or housings
    • 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
    • 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 refrigeration system, and more particularly to a refrigeration system that can efficiently cool a high-temperature portion of a compression refrigerator.
  • a refrigeration cycle in such a refrigeration system can be represented by a Mollier diagram as shown in FIG. 8, for example.
  • a Mollier diagram in the compression refrigeration cycle using carbon dioxide refrigerant shown in Fig. 8, between points 1 and 2 is the compression work of the compressor 101, between points 2 and 3 is heat radiation by the gas cooler 102, between points 3 and 4 and point 7— 1 indicates heat exchange by the internal heat exchanger 103, points 4 and 5 indicate expansion by the expansion valve 104, and points 5 and 6 indicate evaporation by the evaporator 105.
  • Points 6 and 7 are the same in the accumulator 106. It shows gas-liquid separation under pressure.
  • the compressor section as described above becomes high temperature and high pressure, It is desirable to cool appropriately in order to reduce power consumption.
  • a method of cooling the motor with suction gas is known, but in such a method, the degree of superheat of the suction gas is substantially increased (at the same time there is a decrease in gas density). As a result, the power consumption in the compressor may increase and the discharge gas temperature may increase.
  • the discharge gas may be, for example, more than 150 ° C and more than 12MPa, and there is concern about a decrease in durability and strength due to high temperature and pressure. Yes.
  • equipment such as a power pump, which is also known for systems that use sensible heat of brine to cool electrical equipment, etc. (generally, water cooling) is added, and there is a concern about cost, failure risk, and increased energy consumption.
  • the degree of superheat of the suction gas increases (at the same time the gas density decreases) due to the effects of motor waste heat and inverter waste heat, and compression efficiency may decrease. Also, especially in situations where the heat load is small, there is a risk that the amount of circulating refrigerant is small and the motor and inverter will be insufficiently cooled.
  • a thermal siphon is known as a device in which heat is transferred by a phase change of an encapsulating medium without external power, and thereby the equipment can be cooled.
  • Patent Document 1 JP-A-11 193967
  • the object of the present invention is to focus on the problem due to insufficient cooling in the high temperature part of the compression refrigerator as described above, and the characteristics of a thermal siphon capable of cooling a specific part with a simple configuration, and compressing To provide a refrigeration system that can efficiently cool the high-temperature part of a refrigerator to the desired state and shift the operating area to a lower-temperature area by this cooling, thereby significantly improving the efficiency and durability of the refrigeration cycle It is in.
  • a refrigeration system is a closed circuit having a liquid enclosed therein and a liquid evaporation unit and a condensing unit in order to cool a high-temperature part of the compression refrigerator.
  • a thermal siphon that repeats the liquid movement and phase change cycle in a closed circuit is configured so that the liquid inside the evaporation section is heat-received and vaporized, and then liquefied by heat dissipation in the condensation section and returned to the evaporation section. It consists of what is characterized by.
  • thermal siphon what moves heat by phase change of an encapsulated liquid as an encapsulating medium without external power.
  • a thermal siphon As a typical encapsulated liquid, the case of water will be explained. Water boils at 87 ° C under 66661Pa pressure.
  • the thermal siphon can be used on the secondary side of the binary refrigeration system, and further can be used for cooling the compressor on the primary side, for example.
  • the closed circuit is filled with pure water and the pressure is 66661Pa.
  • the boiling temperature of water in this state is 87 ° C.
  • Set the ambient temperature of the condensing part to around 25 ° C, for example.
  • water is distributed to multiple heat exchange pipes by the header part at the bottom of the evaporation part, and the liquid is vaporized. (Latent heat change). Vaporized water with low density rises and flows into the condensing part.
  • the thermal siphon that repeats the cycle of water movement and phase change makes it possible to efficiently cool the high-temperature part of the compression refrigerator, particularly the compressor.
  • the thermal siphon can be configured to have a condensing unit and a full liquid evaporation unit composed of header sections arranged above and below and a plurality of pipe sections that perform heat exchange connecting them.
  • the thermal siphon increases the evaporation amount of the sealed liquid according to the heat load, the heat exchange corresponding to this can be performed in the condensing unit, and the heat exchange amount can be adjusted by the fan air volume, for example.
  • the thermal siphon may be configured such that the evaporation temperature of the liquid can be adjusted by adjusting the internal pressure.
  • a pressure adjustment chamber for adjusting the internal volume is provided in the thermal siphon, and the internal temperature of the thermal siphon is increased or decreased to adjust the cooling temperature.
  • thermoresiphon adjusts the setting of the partition wall made of at least a flexible member, the partition wall support member that elastically changes the stroke in accordance with the pressure in the partition wall, and the stroke setting of the partition wall support member.
  • It is the form which has a pressure regulation chamber provided with the adjusting screw. More specifically, for example, a pressure regulating chamber provided with a partition wall formed of a flexible member such as rubber, a metal bellows, or a metal diaphragm and a partition wall support member (for example, a spring) formed of an elastic member is provided.
  • a pressure regulating chamber provided with a partition wall formed of a flexible member such as rubber, a metal bellows, or a metal diaphragm and a partition wall support member (for example, a spring) formed of an elastic member is provided.
  • the compressor can be a cooling target.
  • an electric motor integrated with the compressor may be included in the high temperature portion of the compression refrigerator that is to be cooled.
  • an inverter that controls the electric motor that drives the compressor may be included in the high temperature portion of the compression chiller that is to be cooled.
  • the compressor section of such a compression refrigerator When the compressor section of such a compression refrigerator is cooled, for example, the compressor may be cooled by the evaporation section of the thermal siphon through the wall surface. With such an arrangement, the compressor as a cooling target is efficiently cooled.
  • the liquid sealed in the thermal siphon in the refrigeration system according to the present invention is not particularly limited as long as the target cooling in the present invention is achieved. It is desirable that the liquid is clearly graspable, and it is desirable that the liquid is water as described above or water. For example, it is preferable that the liquid force contains 50% or more of water.
  • thermal siphons there are those in which a copper or aluminum tube is connected substantially in an endless manner and filled with a refrigerant gas such as carbon dioxide or butane.
  • Evaporative temperature or condensation temperature
  • a thermal siphon is established, the contradiction that the heat load of the compression refrigeration machine becomes higher may occur. Therefore, from this aspect, it is preferable to select a sealed liquid capable of changing the phase of gas and liquid (latent heat change) at an appropriate temperature, for example, a liquid containing 50% or more of water as described above.
  • the refrigerant used in the compression refrigerator in the present invention is not particularly limited. However, in the present invention, the high-temperature portion of the compression refrigerator can be efficiently cooled.
  • the present invention is particularly effective when the refrigeration cycle has a high-temperature and high-pressure part.
  • the present invention is particularly effective when the refrigerant circulating in the compression refrigerator is a refrigerant having a global warming potential (GWP) of 150 or less.
  • GWP global warming potential
  • a compression refrigerator using a refrigerant such as HFC134a can also be a target of the present invention.
  • the refrigeration system according to the present invention does not require any special external power! /, And uses a thermal siphon. Therefore, it is not preferable to install a new power source or the like. It is suitable for a refrigeration system used for an air conditioner.
  • the refrigeration system according to the present invention is not limited to a vehicle air conditioner but can be applied to cooling other devices such as electronic devices.
  • the operation of the present invention will be described for the case where the sealed liquid is water.
  • the lower limit of the housing surface temperature of the compressor is around 90 ° C in the normal operation mode.
  • the force S increases to 160 ° C depending on the conditions.
  • the thermal siphon according to the present invention is activated, the temperature does not rise above the boiling temperature of water in the thermal siphon under any conditions. In other words, proper cooling is performed to prevent an undesirably high temperature.
  • the critical point is as low as about 30 ° C, about 7MPa at a temperature!
  • the dryness at the evaporator inlet is large and the efficiency of the refrigeration system is not good.
  • the internal heat exchanger provided to compensate for this raises the intake gas temperature of the compressor and consequently the discharge gas temperature in order to bring the gas cooler downstream and the piping downstream of the evaporator into contact with each other.
  • a space (jacket) in which water circulates is provided so as to cover the wall surface of the compressor of a compression refrigerator as described later, and connected to the condenser part of the thermal siphon above the jacket by a pipe. Configured to do. Water entering the jacket as a liquid from below is vaporized by the heat of the compressor. At this time, if the pressure force in the jacket is 6661 Pa, the temperature will be kept at 87 ° C, and the high temperature as described above will be surely prevented.
  • the pressure adjusting chamber even if the amount of gas after boiling when the thermal load on the thermal siphon increases, the boiling point does not fluctuate and stable cooling performance can be obtained. become. If this is used for cooling the high-pressure side equipment of a compression refrigeration machine using carbon dioxide refrigerant whose supercritical pressure is on the high-pressure side, the high-pressure side pressure is stable and stable operation is possible without advanced control. It becomes.
  • the thermal siphon is provided and the latent heat at the time of phase change of the liquid sealed in the thermal siphon is used, the boiling determined by the pressure in the closed circuit is used.
  • the temperature of the cooled part can be maintained at a desired constant temperature by the temperature (condensation temperature), and the target cooling can be performed efficiently and reliably.
  • a light alloy material is generally used because of its good formability, good machinability, and high thermal conductivity.
  • light alloys have the property that their strength decreases significantly as the temperature rises.
  • the compressor temperature and the Uzing temperature can be lowered, so that it can be used in a substantially high strength region.
  • thermal siphon Since this thermal siphon has no moving parts, it is extremely reliable and excellent in quietness. In addition, since no special external drive source is required, the present invention can be implemented at low cost and without requiring a large space.
  • the thermal siphon operates at a pressure lower than the atmospheric pressure, the reliability is extremely high even in this aspect where leakage to the outside is eliminated.
  • the high-pressure side heat exchanger of the compression refrigeration machine can be made smaller, and the amount of the enclosed refrigerant can be reduced correspondingly.
  • FIG. 1 is an equipment system diagram when a refrigeration system according to an embodiment of the present invention is applied to a vehicle air conditioner.
  • FIG. 2 is a Mollier fountain diagram of the refrigeration system of FIG.
  • FIG. 3 is a schematic configuration diagram showing a basic configuration of the thermal siphon in FIG. 1.
  • FIG. 4 is a schematic configuration diagram showing an example of a thermal siphon provided with a pressure regulating chamber.
  • FIG. 5 is a schematic longitudinal sectional view of a conventional compressor shown for comparison.
  • FIG. 6 is a schematic longitudinal sectional view of a compressor unit to which the present invention is applied.
  • FIG. 7 is an equipment diagram showing an example of a vehicle air conditioner to which a conventional refrigeration system is applied.
  • FIG. 8 is a Mollier fountain diagram of the refrigeration system of FIG.
  • FIG. 1 shows an equipment layout when a refrigeration system according to an embodiment of the present invention is applied to a vehicle air conditioner.
  • the carbon dioxide refrigerant compressed and discharged by the compressor 11 is sent to the gas cooler 12 and is exchanged with the low pressure refrigerant by the high pressure refrigerant refrigerant internal heat exchanger 13 from the gas cooler 12, and then the expansion valve 14 Then, the refrigerant from the evaporator 15 passes through the accumulator 16, and is then heat-exchanged with the high-pressure side refrigerant by the internal heat exchanger 13 and sucked into the compressor 11.
  • the thermal siphon 17 according to the present invention is provided for the compressor 11 or a part of the compressor 11 of the refrigeration system configured as described above.
  • the thermal siphon 17 includes an evaporation unit 19 for the sealed liquid formed in the form of a jacket 18 around the compressor 11 and a condensing unit 20 positioned above.
  • the evaporating unit 19 is disposed around the compressor 11, but the condensing unit 20 is disposed above the compressor 11.
  • the refrigeration cycle in the refrigeration system including the thermal siphon 17 as described above can be represented by, for example, a Mollier diagram as shown in FIG. In the compression refrigeration cycle using the carbon dioxide refrigerant shown in FIG. 2, boiling cooling of the liquid sealed in the thermal siphon 17 is used for cooling the compressor 11. In Figure 2, point 1 one!
  • the interval between ' ⁇ 2 is equivalent to the compression work by the compressor 11 (virtual component), but due to the boiling cooling by the thermal siphon 17, the compressor 11 is cooled as between the points 1' 2 'and the compressor 1 The high temperature of 1 is prevented.
  • heat is dissipated by gas cooler 12, between points 3 and 4 and between points 7 and 1, heat is exchanged by internal heat exchanger 13, between points 4 and 5 is expansion by expansion valve 14, and points 5 and 6
  • the intervals indicate evaporation by the evaporator 15, and points 6 and 7 indicate gas-liquid separation in the accumulator 16 under the same pressure state.
  • the compressor 11 is efficiently cooled by the thermal siphon 17 even on the Mollier diagram. If the point 2 ′ is at the point 3, the gas cooler Omission of 12 is also possible.
  • the thermal siphon 17 has a basic configuration as shown in FIG. 3, for example.
  • the evaporation section 19 in which the sealed liquid flows in the liquid phase is located on the lower side, and the condensing section 20 in which the sealed liquid flows in the gas phase and is liquefied by heat dissipation is arranged above it! /
  • These are configured in a closed circuit, and after the liquid inside the evaporation unit 19 has received heat and vaporized, the liquid moves in the closed circuit so that it is liquefied by heat dissipation in the condensation unit 20 and returned to the evaporation unit 19.
  • phase change cycle is repeated, and the high temperature part of the compression refrigerator is cooled by the endothermic heat generated by vaporization (latent heat change) in the evaporation part 19.
  • the thermal siphon 17 circulates the sealed liquid without applying any special external power.
  • FIG. 4 illustrates the case where the pressure regulating chamber 21 is provided in the thermal siphon 17.
  • the pressure regulating chamber 21 is made of a flexible member, and a rubber or metal bellows 22 as a partition wall through which the sealed liquid in the thermal siphon 17 circulates, and the pressure in the bellows 22.
  • a spring 23 as a partition wall supporting member that changes the stroke in response to inertia and an adjusting screw 24 for adjusting the setting of the stroke of the spring 23 are provided.
  • the difference between the pressure inside the bellows 22 and the atmospheric pressure may be balanced by the spring 23 and the adjusting screw 24. 100 ° C water When boiling above, the installation of the spring 23 is reversed.
  • FIG. 5 shows an example of a conventional compressor 31 for comparison.
  • the compressor 31 is formed by integrating a compression mechanism 32 and an electric motor 33 (for example, a DC brushless motor) that drives the compression mechanism 32, and the electric motor 33 is controlled by an inverter 34.
  • the suction refrigerant 35 is sucked into the compression mechanism 32 through the electric motor 33, thereby cooling the electric motor 33 together with the compressor 31.
  • the refrigerant compressed by the compression mechanism 32 is discharged as the compressed refrigerant 36.
  • FIG. 6 shows the configuration of the compressor 11 shown in FIG. 1 and its surroundings.
  • the compressor 11 is driven by an electric motor 42 with a built-in compression mechanism 41.
  • the force suction refrigerant 43 is directly passed through the electric motor 42 without passing through it.
  • the refrigerant introduced into the compression mechanism 41 and compressed by the compression mechanism 41 is discharged as the compressed refrigerant 44.
  • the evaporator 11 of the thermal siphon 17 is arranged with respect to the compressor 11 in the structure of the jacket 18 described above, and the sealed liquid is circulated between the evaporator 19 and the condenser 20.
  • the jacket 18 for cooling is arranged so that the electric motor 42 part can be cooled by covering the electric motor 42 part, and the inverter 45 that controls the electric motor 42 can also be cooled.
  • the compressor 11, the electric motor 42, and the inverter 45 are all cooled efficiently.
  • the above embodiment is a force S exemplifying the case where the present invention is applied to cooling of a compressor portion in a vehicle-mounted air conditioner, and the present invention is applicable to other parts of the apparatus, Furthermore, it is applicable not only to a vehicle-mounted air conditioner but also to other refrigeration systems.
  • the refrigeration system according to the present invention is used at room temperature, and can be cooled to a room temperature level. Suitable for required applications. For example, it is suitable for cooling electronic devices and compressors constituting a compression refrigerator.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Air-Conditioning For Vehicles (AREA)
  • Compressor (AREA)

Abstract

A refrigeration system formed as a closed circuit to cool a high-temperature portion of a compression refrigeration machine, the closed circuit having liquid sealed in it and being provided with an evaporation section and condensation section for the liquid. The refrigeration circuit is provided with a thermal siphon for repeating a cycle of movement and phase change of the liquid in the closed circuit such that, after the liquid in the evaporation section receives heat and is evaporated, it is liquefied by heat radiation in the condensation section and returned to the evaporation section. The high-temperature section of the compression refrigeration machine can be efficiently cooled to a desired level, and the cooling shifts a use region to a region of a lower temperature to significantly increase efficiency and durability of the refrigeration cycle.

Description

明 細 書  Specification

冷凍システム  Refrigeration system

技術分野  Technical field

[0001] 本発明は、冷凍システムに関し、とくに、圧縮式冷凍機の高温部を効率よく冷却で きるようにした冷凍システムに関する。  TECHNICAL FIELD [0001] The present invention relates to a refrigeration system, and more particularly to a refrigeration system that can efficiently cool a high-temperature portion of a compression refrigerator.

背景技術  Background art

[0002] 近年開発が盛んになつている二酸化炭素冷媒を用いた圧縮式冷凍機では、成績 係数 COPを良好に確保するために、冷凍サイクル内に内部熱交換器を設けるのが 一般的になっている(例えば、特許文献 1)。しかし、このような冷凍サイクルにおいて は、圧縮機の吸入ガス温度が高いことと二酸化炭素冷媒の比熱比が大きいことにより 吐出ガス温度が非常に高ぐ圧縮機の消費動力が大きぐ圧縮機全体として高温高 圧に対応した材質選定や強度確保が必要であり、コストや生産性を悪化させる要因 となっていた。  [0002] In compression chillers using carbon dioxide refrigerant, which has been actively developed in recent years, it is common to provide an internal heat exchanger in the refrigeration cycle in order to ensure a good coefficient of performance COP. (For example, Patent Document 1). However, in such a refrigeration cycle, the compressor has a high intake gas temperature and a large specific heat ratio of the carbon dioxide refrigerant. It was necessary to select materials and ensure strength to cope with high temperature and high pressure, which caused cost and productivity deterioration.

[0003] 従来の二酸化炭素冷媒を使用した冷凍システムは、例えば図 7に車両用空調装置 における冷凍システムの場合の例を示すように、圧縮機 101で圧縮され吐出された 二酸化炭素冷媒がガスクーラ 102に送られ、ガスクーラ 102からの高圧側冷媒カ 内 部熱交換器 103により低圧側冷媒と熱交換された後、膨張弁 104を介して蒸発器 10 5に送られ、蒸発器 105からの冷媒がアキュムレータ 106を通した後、内部熱交換器 103により高圧側冷媒と熱交換され、圧縮機 101に吸入される。  [0003] In a conventional refrigeration system using carbon dioxide refrigerant, for example, as shown in FIG. 7 as an example of a refrigeration system in a vehicle air conditioner, carbon dioxide refrigerant compressed and discharged by a compressor 101 is gas cooler 102. After the heat exchange with the low-pressure side refrigerant by the high-pressure side refrigerant internal heat exchanger 103 from the gas cooler 102, the refrigerant is sent to the evaporator 105 via the expansion valve 104, and the refrigerant from the evaporator 105 is After passing through the accumulator 106, the internal heat exchanger 103 exchanges heat with the high-pressure side refrigerant and sucks it into the compressor 101.

[0004] このような冷凍システムにおける冷凍サイクルは、例えば図 8に示すようなモリエル 線図で表すことができる。図 8に示した二酸化炭素冷媒を使用した圧縮冷凍サイクル においては、ポイント 1—2間が圧縮機 101の圧縮仕事、ポイント 2— 3間がガスクーラ 102による放熱、ポイント 3— 4間およびポイント 7—1間が内部熱交換器 103による熱 交換、ポイント 4— 5間が膨張弁 104による膨張、ポイント 5— 6間が蒸発器 105による 蒸発をそれぞれ示しており、ポイント 6、 7はアキュムレータ 106における同圧状態で の気液分離を示している。  [0004] A refrigeration cycle in such a refrigeration system can be represented by a Mollier diagram as shown in FIG. 8, for example. In the compression refrigeration cycle using carbon dioxide refrigerant shown in Fig. 8, between points 1 and 2 is the compression work of the compressor 101, between points 2 and 3 is heat radiation by the gas cooler 102, between points 3 and 4 and point 7— 1 indicates heat exchange by the internal heat exchanger 103, points 4 and 5 indicate expansion by the expansion valve 104, and points 5 and 6 indicate evaporation by the evaporator 105. Points 6 and 7 are the same in the accumulator 106. It shows gas-liquid separation under pressure.

[0005] このような冷凍システムにおいては、上述の如ぐ圧縮機部が高温高圧となるので、 消費動力低減等のために適切に冷却されることが望ましい。また、電動モータで駆動 される圧縮機については、吸入ガスによりモータを冷却する方式が知られているが、 そのような方式では、実質的に吸入ガス過熱度が上がり(同時にガス密度低下もあり) 、結果的に圧縮機での消費動力の増大や吐出ガス温度の上昇が生じることがあった 。また、効率よくモータを駆動するためモータをインバータ駆動する方式もある力 こ のインバータについても冷却が必要であり、上述のモータと同様の問題が生じること があった。 [0005] In such a refrigeration system, the compressor section as described above becomes high temperature and high pressure, It is desirable to cool appropriately in order to reduce power consumption. For compressors driven by an electric motor, a method of cooling the motor with suction gas is known, but in such a method, the degree of superheat of the suction gas is substantially increased (at the same time there is a decrease in gas density). As a result, the power consumption in the compressor may increase and the discharge gas temperature may increase. In addition, there is a method of driving the motor with an inverter in order to drive the motor efficiently. This inverter also needs to be cooled, and the same problem as the motor described above may occur.

[0006] 圧縮機の冷却、特に二酸化炭素冷媒を使うシステムでは、吐出ガスは例えば 150 °C超、 12MPa超となることがあり、高温高圧に起因する耐久性低下や強度低下が懸 念されている。また、電気機器等の冷却をブラインの顕熱を使ったシステム(一般的 には水冷)も知られている力 ポンプ等の機器が追加となり、コストや故障リスクおよび 消費エネルギーの増加が懸念される。さらに、電動モーター体型の圧縮機では、モ ータ廃熱やインバータ廃熱の影響を受けて吸入ガスの過熱度が高くなり(同時にガス 密度が小さくなり)、圧縮効率が低下するおそれがある。また、特に熱負荷の小さい 状況では、循環冷媒量が少なくモータやインバータの冷却が不十分になるおそれが ある。  [0006] In a cooling system for a compressor, particularly in a system using a carbon dioxide refrigerant, the discharge gas may be, for example, more than 150 ° C and more than 12MPa, and there is concern about a decrease in durability and strength due to high temperature and pressure. Yes. In addition, equipment such as a power pump, which is also known for systems that use sensible heat of brine to cool electrical equipment, etc. (generally, water cooling) is added, and there is a concern about cost, failure risk, and increased energy consumption. . Furthermore, in an electric motor type compressor, the degree of superheat of the suction gas increases (at the same time the gas density decreases) due to the effects of motor waste heat and inverter waste heat, and compression efficiency may decrease. Also, especially in situations where the heat load is small, there is a risk that the amount of circulating refrigerant is small and the motor and inverter will be insufficiently cooled.

[0007] 一方、外部動力なしで封入媒体の相変化によって熱の移動を行い、それによつて 機器の冷却が可能なものとして、サーマルサイフォンが知られている。しかし、圧縮式 冷凍機構成の冷凍システムに、サーマルサイフォンを適用した例は見当たらない。 特許文献 1 :特開平 11 193967号公報  [0007] On the other hand, a thermal siphon is known as a device in which heat is transferred by a phase change of an encapsulating medium without external power, and thereby the equipment can be cooled. However, there are no examples of applying a thermal siphon to a refrigeration system with a compression chiller configuration. Patent Document 1: JP-A-11 193967

発明の開示  Disclosure of the invention

発明が解決しょうとする課題  Problems to be solved by the invention

[0008] そこで本発明の課題は、上記のような圧縮式冷凍機の高温部における冷却不足に 伴う問題と、簡素な構成で特定部位の冷却が可能なサーマルサイフォンの特性に着 目し、圧縮式冷凍機の高温部を効率よく所望の状態まで冷却でき、該冷却により使 用領域をより低温領域にシフトさせて冷凍サイクルの効率や耐久性を大幅に向上可 能な冷凍システムを提供することにある。 [0008] Therefore, the object of the present invention is to focus on the problem due to insufficient cooling in the high temperature part of the compression refrigerator as described above, and the characteristics of a thermal siphon capable of cooling a specific part with a simple configuration, and compressing To provide a refrigeration system that can efficiently cool the high-temperature part of a refrigerator to the desired state and shift the operating area to a lower-temperature area by this cooling, thereby significantly improving the efficiency and durability of the refrigeration cycle It is in.

課題を解決するための手段 [0009] 上記課題を解決するために、本発明に係る冷凍システムは、圧縮式冷凍機の高温 部を冷却するために、液体が封入され該液体の蒸発部と凝縮部とを有する閉回路に 構成され、蒸発部内部の液体が受熱気化した後、凝縮部での放熱により液化し蒸発 部に帰還するように、閉回路で液体の移動と相変化のサイクルを繰り返すサーマル サイフォンを設けたことを特徴とするものからなる。 Means for solving the problem [0009] In order to solve the above problems, a refrigeration system according to the present invention is a closed circuit having a liquid enclosed therein and a liquid evaporation unit and a condensing unit in order to cool a high-temperature part of the compression refrigerator. A thermal siphon that repeats the liquid movement and phase change cycle in a closed circuit is configured so that the liquid inside the evaporation section is heat-received and vaporized, and then liquefied by heat dissipation in the condensation section and returned to the evaporation section. It consists of what is characterized by.

[0010] ここで、外部動力なしで封入媒体としての封入液体の相変化によって熱の移動を 行うものをサーマルサイフォンと呼ぶ。代表的な封入液体として、水の場合について 説明するに、水は 66661Paの圧力下では 87°Cで沸騰する。これをサーマルサイフォ ン閉回路中で利用することにより、 87°C以上に発熱する機器を 87°Cにまで無動力で 冷却することが可能となる(ただし、サーマルサイフォンシステムとの熱交換効率が 10 0%と仮定)。つまり、サーマルサイフォンを二元冷凍システムの二次側に使用するこ ともできるし、更には一次側の例えば圧縮機の冷却に使用することもできる。  [0010] Here, what moves heat by phase change of an encapsulated liquid as an encapsulating medium without external power is called a thermal siphon. As a typical encapsulated liquid, the case of water will be explained. Water boils at 87 ° C under 66661Pa pressure. By utilizing this in the closed circuit of the thermal siphon, it becomes possible to cool equipment that generates heat above 87 ° C to 87 ° C without power (however, the efficiency of heat exchange with the thermal siphon system is high). Assuming 100%). In other words, the thermal siphon can be used on the secondary side of the binary refrigeration system, and further can be used for cooling the compressor on the primary side, for example.

[0011] 例えば閉回路内を純粋な水で満たし圧力を 66661Paとする。この状態での水の沸 騰温度は 87°Cである。凝縮部の雰囲気温度を例えば 25°C前後とする。冷却を必要と する機器の温度が 87°Cを超える状態でこれに接するサーマルサイフォンの蒸発部内 部では、例えば蒸発部下部のヘッダー部により複数の熱交換管部に水が分配され、 液体が気化 (潜熱変化)する。気化し密度が小さくなつた水は、上昇して凝縮部に流 入する。蒸発部内部で液体が残った場合には、蒸発部内上部のヘッダー部タンク内 に液面が形成されて下方に滞留し、凝縮部へは流出しないようになっている。水は凝 縮部で放熱後液化し、重力により蒸発部に帰還する。このような水の移動と相変化の サイクルを繰り返すサーマルサイフォンにより、圧縮式冷凍機の高温部、とくに圧縮 機の冷却を効率よく行うことが可能になる。なお、サーマルサイフォンは、上下に配置 されたヘッダー部とそれらをつなぐ熱交換を行う複数の管部とで構成された凝縮部お よび満液式蒸発部を備えた構造に構成できる。そして、サーマルサイフォンは熱負荷 に応じて封入液体の蒸発量が増すため、これに応じた熱交換を凝縮部で行い、例え ばファン風量によりその熱交換量を調整するようにすることもできる。この場合、凝縮 部を圧縮式冷凍機の高圧側熱交換器の上方に並べて配置し、共通のファンで冷却 するようにしてあよレヽ。 [0012] この本発明に係る冷凍システムにおいては、上記サーマルサイフォンは内圧を調整 することにより液体の蒸発温度が調整可能に構成されている形態とすることもできる。 例えば、サーマルサイフォンに、その内容積を調整する調圧室を設け、サーマルサイ フォン内圧を増減し、冷却温度を調整するのである。具体的には、例えば、サーマノレ サイフォンが、少なくとも可撓性部材よりなる隔壁と、隔壁内の圧力に応じて弾性的に ストロークを変える隔壁支持部材と、隔壁支持部材のストロークの設定を調整する調 整ねじを備えた調圧室を有する形態である。より具体的には、例えば、ゴムや金属べ ローズ、金属ダイアフラム等の可撓性部材で形成された隔壁と弾性部材で形成され た隔壁支持部材 (例えば、スプリング)を備えた調圧室を設け、水を 100°C以下で沸 騰させる場合には隔壁内圧力と大気圧の差圧分をスプリングおよび調整ねじでバラ ンスさせる。水を 100°C以上で沸騰させる場合にはスプリングの取付け方が逆になる [0011] For example, the closed circuit is filled with pure water and the pressure is 66661Pa. The boiling temperature of water in this state is 87 ° C. Set the ambient temperature of the condensing part to around 25 ° C, for example. In the inside of the evaporation part of the thermal siphon that comes into contact with the equipment that needs to be cooled when the temperature exceeds 87 ° C, for example, water is distributed to multiple heat exchange pipes by the header part at the bottom of the evaporation part, and the liquid is vaporized. (Latent heat change). Vaporized water with low density rises and flows into the condensing part. When liquid remains in the evaporation section, a liquid surface is formed in the header tank in the upper part of the evaporation section and stays below, so that it does not flow out to the condensation section. Water is liquefied after heat dissipation in the condensation section and returns to the evaporation section by gravity. The thermal siphon that repeats the cycle of water movement and phase change makes it possible to efficiently cool the high-temperature part of the compression refrigerator, particularly the compressor. Note that the thermal siphon can be configured to have a condensing unit and a full liquid evaporation unit composed of header sections arranged above and below and a plurality of pipe sections that perform heat exchange connecting them. Since the thermal siphon increases the evaporation amount of the sealed liquid according to the heat load, the heat exchange corresponding to this can be performed in the condensing unit, and the heat exchange amount can be adjusted by the fan air volume, for example. In this case, arrange the condensers side by side above the high-pressure heat exchanger of the compression refrigerator and cool with a common fan. [0012] In the refrigeration system according to the present invention, the thermal siphon may be configured such that the evaporation temperature of the liquid can be adjusted by adjusting the internal pressure. For example, a pressure adjustment chamber for adjusting the internal volume is provided in the thermal siphon, and the internal temperature of the thermal siphon is increased or decreased to adjust the cooling temperature. Specifically, for example, a thermoresiphon adjusts the setting of the partition wall made of at least a flexible member, the partition wall support member that elastically changes the stroke in accordance with the pressure in the partition wall, and the stroke setting of the partition wall support member. It is the form which has a pressure regulation chamber provided with the adjusting screw. More specifically, for example, a pressure regulating chamber provided with a partition wall formed of a flexible member such as rubber, a metal bellows, or a metal diaphragm and a partition wall support member (for example, a spring) formed of an elastic member is provided. When boiling water below 100 ° C, balance the pressure difference between the pressure inside the partition wall and atmospheric pressure with a spring and adjusting screw. If water is boiled at 100 ° C or higher, the spring mounting method is reversed.

[0013] 上記サーマルサイフォンにより冷却される圧縮式冷凍機の高温部としては、とくに圧 縮機を冷却対象とできる。また、冷却対象となる圧縮式冷凍機の高温部に、圧縮機 に一体に組み込まれた電動モータを含めてもよい。さらに、冷却対象となる圧縮式冷 凍機の高温部に、圧縮機を駆動する電動モータを制御するインバータを含めてもよ い。 [0013] As a high-temperature portion of the compression refrigerator that is cooled by the thermal siphon, the compressor can be a cooling target. In addition, an electric motor integrated with the compressor may be included in the high temperature portion of the compression refrigerator that is to be cooled. Furthermore, an inverter that controls the electric motor that drives the compressor may be included in the high temperature portion of the compression chiller that is to be cooled.

[0014] このような圧縮式冷凍機の圧縮機部を冷却する場合には、例えば、該圧縮機がそ の壁面を介して、サーマルサイフォンの蒸発部により冷却されるようにすればよい。こ のような配置により、冷却対象としての圧縮機が効率よく冷却される。  [0014] When the compressor section of such a compression refrigerator is cooled, for example, the compressor may be cooled by the evaporation section of the thermal siphon through the wall surface. With such an arrangement, the compressor as a cooling target is efficiently cooled.

[0015] また、本発明に係る冷凍システムにおけるサーマルサイフォンに封入される液体と しては、本発明で目標とする冷却が達成される限りとくに限定されないが、取扱いが 容易であり、特性を予め明瞭に把握できる液体であることが望ましぐ前述の如ぐ水 あるいは水を主体とする液体であることが望ましい。例えば、水を 50%以上含む液体 力もなることが好ましい。  [0015] In addition, the liquid sealed in the thermal siphon in the refrigeration system according to the present invention is not particularly limited as long as the target cooling in the present invention is achieved. It is desirable that the liquid is clearly graspable, and it is desirable that the liquid is water as described above or water. For example, it is preferable that the liquid force contains 50% or more of water.

[0016] また、サーマルサイフォンとしては、銅又はアルミニウム管を実質的にエンドレス状 につないだものに、二酸化炭素又はブタン等の冷媒ガスを充填したものも存在してい たが、例えば二酸化炭素の実質的な蒸発温度(あるいは凝縮温度)は 8°Cと常温 域になくサーマルサイフォンが成立するためにかえって圧縮式冷凍機の熱負荷が高 くなるという矛盾が生じてくるおそれがある。したがって、このような面からも、適切な温 度で気液の相変化(潜熱変化)が可能な封入液体、例えば上記の如く水を 50%以 上含む液体、を選定することが好ましい。 [0016] Further, as thermal siphons, there are those in which a copper or aluminum tube is connected substantially in an endless manner and filled with a refrigerant gas such as carbon dioxide or butane. Evaporative temperature (or condensation temperature) is 8 ° C, normal temperature Since a thermal siphon is established, the contradiction that the heat load of the compression refrigeration machine becomes higher may occur. Therefore, from this aspect, it is preferable to select a sealed liquid capable of changing the phase of gas and liquid (latent heat change) at an appropriate temperature, for example, a liquid containing 50% or more of water as described above.

[0017] 本発明における圧縮式冷凍機に使用される冷媒としても特に限定はしないが、本 発明では圧縮式冷凍機の高温部を効率よく冷却できることから、冷媒が二酸化炭素 力もなる場合に、つまり、冷凍サイクル中に高温高圧部を有する場合に、とくに本発 明は効果的である。あるいは別の表現をすれば、圧縮式冷凍機内を循環する冷媒が 、地球温暖化係数 (GWP) 150以下の冷媒である場合、本発明はとくに効果的であ る。ただし、 HFC134a等の冷媒を使用する圧縮式冷凍機も、本発明の対象とするこ と力 Sできる。 [0017] The refrigerant used in the compression refrigerator in the present invention is not particularly limited. However, in the present invention, the high-temperature portion of the compression refrigerator can be efficiently cooled. The present invention is particularly effective when the refrigeration cycle has a high-temperature and high-pressure part. In other words, the present invention is particularly effective when the refrigerant circulating in the compression refrigerator is a refrigerant having a global warming potential (GWP) of 150 or less. However, a compression refrigerator using a refrigerant such as HFC134a can also be a target of the present invention.

[0018] また、本発明に係る冷凍システムにおいては、とくに、上記サーマルサイフォンによ り圧縮式冷凍機の圧縮機動力相当分の熱交換が行われることが好まし!/、。このように すれば、後述のモリエル線図で説明するように、極めて効率のよい冷凍サイクルの実 現が可能になり、場合によっては、従来サイクルにおけるガスクーラを省略できる可 能性まで生じてくる。  [0018] Further, in the refrigeration system according to the present invention, it is particularly preferable that heat exchange corresponding to the compressor power of the compression chiller is performed by the thermal siphon! /. This makes it possible to realize a very efficient refrigeration cycle, as described in the Mollier diagram described later, and in some cases, the possibility of omitting the gas cooler in the conventional cycle arises.

[0019] また、本発明に係る冷凍システムは、特別な外部動力を要しな!/、サーマルサイフォ ンを利用したものであるから、とくに新たな動力源等の搭載が好まれない、車両用空 調装置に用いられる冷凍システム等に好適なものである。ただし、本発明に係る冷凍 システムは、車両用空調装置に限らず、他の装置、例えば電子機器等の冷却にも適 用可能である。  [0019] In addition, the refrigeration system according to the present invention does not require any special external power! /, And uses a thermal siphon. Therefore, it is not preferable to install a new power source or the like. It is suitable for a refrigeration system used for an air conditioner. However, the refrigeration system according to the present invention is not limited to a vehicle air conditioner but can be applied to cooling other devices such as electronic devices.

[0020] 本発明における作用を、封入液体が水の場合について説明するに、例えば車両用 空調装置の場合、通常の運転モードでは圧縮機のハウジング表面温度の下限は 90 °C前後で、圧縮機の回転速度が高まるにつれて上昇し条件によっては 160°Cにまで 達すること力 Sある。し力、し本発明におけるサーマルサイフォンが作動すると、どのよう な条件であってもサーマルサイフォン内での水の沸騰温度以上に温度が上昇するこ とはない。つまり、望ましくない高温化を防止するために、適切な冷却が行われること になる。 [0021] 冷媒に二酸化炭素を用いた圧縮式冷凍機の場合には、臨界点が約 30°Cという低 V、温度で約 7MPaと!/、う高!/、圧力であると!/、う冷媒の特性があり、通常の内部熱交換 器を使わな!/、サイクル構成では蒸発器入口での乾き度が大きく冷凍システムとしての 効率が良くない。これを補うため設けられた内部熱交換器は、ガスクーラ下流と蒸発 器下流の配管を接触させるため、圧縮機の吸入ガス温度を上昇させ、ひいては吐出 ガス温度も上昇させる。本発明では、例えば後述の如ぐ圧縮式冷凍機の圧縮機の 壁面を覆うように水が循環する空間(ジャケット)を設け、該ジャケットより上方にあるサ 一マルサイフォンの凝縮部と配管で接続するように構成される。ジャケット内に下方か ら液体として入ってきた水は圧縮機の熱を受け気化する。このときジャケット内の圧力 力 6661Paであれば温度は 87°Cに保たれることになり、前述のような高温に至ることは 確実に防止される。 [0020] The operation of the present invention will be described for the case where the sealed liquid is water. For example, in the case of a vehicle air conditioner, the lower limit of the housing surface temperature of the compressor is around 90 ° C in the normal operation mode. As the rotation speed increases, the force S increases to 160 ° C depending on the conditions. When the thermal siphon according to the present invention is activated, the temperature does not rise above the boiling temperature of water in the thermal siphon under any conditions. In other words, proper cooling is performed to prevent an undesirably high temperature. [0021] In the case of a compression refrigerator using carbon dioxide as a refrigerant, the critical point is as low as about 30 ° C, about 7MPa at a temperature! Due to the characteristics of the refrigerant, do not use a normal internal heat exchanger! / In the cycle configuration, the dryness at the evaporator inlet is large and the efficiency of the refrigeration system is not good. The internal heat exchanger provided to compensate for this raises the intake gas temperature of the compressor and consequently the discharge gas temperature in order to bring the gas cooler downstream and the piping downstream of the evaporator into contact with each other. In the present invention, for example, a space (jacket) in which water circulates is provided so as to cover the wall surface of the compressor of a compression refrigerator as described later, and connected to the condenser part of the thermal siphon above the jacket by a pipe. Configured to do. Water entering the jacket as a liquid from below is vaporized by the heat of the compressor. At this time, if the pressure force in the jacket is 6661 Pa, the temperature will be kept at 87 ° C, and the high temperature as described above will be surely prevented.

[0022] また、調圧室を設けることにより、サーマルサイフォンに対する熱負荷が増加した際 に沸騰した後の気体の量が増加しても、沸点が変動せず安定した冷却性能が得られ るようになる。これを、高圧側が超臨界となる二酸化炭素冷媒を使った圧縮式冷凍機 の高圧側機器の冷却に用いると、高圧側圧力が安定し、高度な制御をしなくても安 定した運転が可能となる。  [0022] Further, by providing the pressure adjusting chamber, even if the amount of gas after boiling when the thermal load on the thermal siphon increases, the boiling point does not fluctuate and stable cooling performance can be obtained. become. If this is used for cooling the high-pressure side equipment of a compression refrigeration machine using carbon dioxide refrigerant whose supercritical pressure is on the high-pressure side, the high-pressure side pressure is stable and stable operation is possible without advanced control. It becomes.

発明の効果  The invention's effect

[0023] このように、本発明に係る冷凍システムによれば、サーマルサイフォンを設けてそれ に封入された液体の相変化の際の潜熱を利用するため、閉回路内の圧力により決定 される沸騰温度 (凝縮温度)で被冷却部の温度を所望の一定温度に保つことが可能 になり、 目標とする冷却が効率よく確実に行われることになる。  As described above, according to the refrigeration system of the present invention, since the thermal siphon is provided and the latent heat at the time of phase change of the liquid sealed in the thermal siphon is used, the boiling determined by the pressure in the closed circuit is used. The temperature of the cooled part can be maintained at a desired constant temperature by the temperature (condensation temperature), and the target cooling can be performed efficiently and reliably.

[0024] また、圧縮式冷凍機の圧縮機のハウジングに関しては、成形性や切削性の良さや 熱伝導率の高さから軽合金材料が一般的に使用されている。しかし軽合金は高温に なるにつれて強度が著しく低下する特性がある。本発明による冷却の結果、圧縮機 ノ、ウジング温度を低下させることができるので、実質的に高い強度の領域での使用 が可能となる。  [0024] For the compressor housing of the compression refrigerator, a light alloy material is generally used because of its good formability, good machinability, and high thermal conductivity. However, light alloys have the property that their strength decreases significantly as the temperature rises. As a result of the cooling according to the present invention, the compressor temperature and the Uzing temperature can be lowered, so that it can be used in a substantially high strength region.

[0025] また、サーマルサイフォンの温度を一定に保つ冷却特性を活かせば、シール材質 の高温劣化も防止できる。 [0026] また、サーマルサイフォンの温度を一定に保つ冷却特性を活かせば、冷凍機油粘 度低下防止により潤滑油膜厚が確保されるので、シール摺動部や軸受け部の耐久 性を向上することもできる。 [0025] Further, by utilizing the cooling characteristic that keeps the temperature of the thermal siphon constant, deterioration of the seal material at high temperature can be prevented. [0026] Further, if the cooling characteristics that keep the temperature of the thermal siphon constant are utilized, the lubricating oil film thickness is secured by preventing the refrigeration machine oil viscosity from being lowered, so that the durability of the seal sliding part and the bearing part can be improved. it can.

[0027] このサーマルサイフォンは可動部を持たないため極めて信頼性が高ぐ静粛性にも 優れている。また、特別な外部駆動源も必要としないため、安価にかつ大きなスぺー スを要することなく本発明を実施できる。 [0027] Since this thermal siphon has no moving parts, it is extremely reliable and excellent in quietness. In addition, since no special external drive source is required, the present invention can be implemented at low cost and without requiring a large space.

[0028] また、サーマルサイフォンは大気圧よりも低い圧力で作動するため、外部に対する 漏れがなぐこの面でも極めて信頼性が高い。 [0028] Further, since the thermal siphon operates at a pressure lower than the atmospheric pressure, the reliability is extremely high even in this aspect where leakage to the outside is eliminated.

[0029] また、サーマルサイフォンによる適切な冷却により、圧縮式冷凍機の高圧側熱交換 器を小さくすることが可能になり、その分封入冷媒量を低減することも可能になる。 [0029] Further, by appropriate cooling by the thermal siphon, the high-pressure side heat exchanger of the compression refrigeration machine can be made smaller, and the amount of the enclosed refrigerant can be reduced correspondingly.

[0030] さらに、熱負荷の少な!/、状況で例えば電動モーター体の圧縮機を備えた圧縮式冷 凍機を使用する場合であっても、圧縮機の性能や耐久性の低下が無!/、。 [0030] Furthermore, even when using a compression refrigeration machine equipped with a compressor with an electric motor body in a low heat load! / Situation, there is no decrease in the performance and durability of the compressor! /.

図面の簡単な説明  Brief Description of Drawings

[0031] [図 1]本発明の一実施態様に係る冷凍システムを車両用空調装置に適用した場合の 機器系統図である。  FIG. 1 is an equipment system diagram when a refrigeration system according to an embodiment of the present invention is applied to a vehicle air conditioner.

[図 2]図 1の冷凍システムのモリエル泉図である。  FIG. 2 is a Mollier fountain diagram of the refrigeration system of FIG.

[図 3]図 1におけるサーマルサイフォンの基本構成を示す概略構成図である。  FIG. 3 is a schematic configuration diagram showing a basic configuration of the thermal siphon in FIG. 1.

[図 4]調圧室を備えたサーマルサイフォンの一例を示す概略構成図である。  FIG. 4 is a schematic configuration diagram showing an example of a thermal siphon provided with a pressure regulating chamber.

[図 5]比較のために示した従来の圧縮機の概略縦断面図である。  FIG. 5 is a schematic longitudinal sectional view of a conventional compressor shown for comparison.

[図 6]本発明を適用した圧縮機部の概略縦断面図である。  FIG. 6 is a schematic longitudinal sectional view of a compressor unit to which the present invention is applied.

[図 7]従来の冷凍システムを適用した車両用空調装置の一例を示す機器系統図であ  FIG. 7 is an equipment diagram showing an example of a vehicle air conditioner to which a conventional refrigeration system is applied.

[図 8]図 7の冷凍システムのモリエル泉図である。 FIG. 8 is a Mollier fountain diagram of the refrigeration system of FIG.

符号の説明  Explanation of symbols

[0032] 11 圧縮機 [0032] 11 Compressor

12 ガスクーラ  12 Gas cooler

13 内部熱交換器  13 Internal heat exchanger

14 膨張弁 15 蒸発器 14 Expansion valve 15 Evaporator

16 アキュムレータ  16 Accumulator

17 サーマノレサイフォン  17 Thermore Siphon

18 ジャケット  18 jacket

19 蒸発部  19 Evaporator

20 凝縮部  20 Condensing section

21 調圧室  21 Pressure control chamber

22 隔壁としてのベローズ  22 Bellows as a bulkhead

23 隔壁支持部材としてのスプリ グ  23 Spring as a bulkhead support member

24 調整ねじ  24 Adjustment screw

41 圧縮機構  41 Compression mechanism

42 電動モータ  42 Electric motor

43 吸入冷媒  43 Suction refrigerant

44 圧縮冷媒  44 Compressed refrigerant

45 インバータ  45 Inverter

発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION

以下に、本発明の望ましい実施の形態を、図面を参照して説明する。  Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.

図 1は、本発明の一実施態様に係る冷凍システムを車両用空調装置に適用した場 合の機器配置を示している。図 1において、圧縮機 11で圧縮され吐出された二酸化 炭素冷媒がガスクーラ 12に送られ、ガスクーラ 12からの高圧側冷媒カ 内部熱交換 器 13により低圧側冷媒と熱交換された後、膨張弁 14を介して蒸発器 15に送られ、 蒸発器 15からの冷媒がアキュムレータ 16を通した後、内部熱交換器 13により高圧側 冷媒と熱交換され、圧縮機 11に吸入される。このように構成された冷凍システムの圧 縮機 11、または圧縮機 11の一部分に対して、本発明におけるサーマルサイフォン 1 7が設けられている。このサーマルサイフォン 17は、圧縮機 11の周囲にジャケット 18 の形態に形成された封入液体の蒸発部 19と、上方に位置する凝縮部 20とを備えて いる。蒸発部 19は、圧縮機 11の周囲に配置されるが、凝縮部 20は、圧縮機 11よりも 上方に配置されている。 [0034] 上記のようにサーマルサイフォン 17を備えた冷凍システムにおける冷凍サイクルは 、例えば図 2に示すようなモリエル線図で表すことができる。図 2に示した二酸化炭素 冷媒を使用した圧縮冷凍サイクルにおいては、サーマルサイフォン 17に封入された 液体の沸騰冷却が圧縮機 11の冷却に利用される。図 2において、ポイント 1一;!'〜 2 間が圧縮機 11によるの圧縮仕事相当分 (仮想分)であるが、サーマルサイフォン 17 による沸騰冷却により、ポイント 1 ' 2'間のように、圧縮機 11が冷却されて圧縮機 1 1の高温化が防止されている。ポイント 2'—3間はガスクーラ 12による放熱、ポイント 3 —4間およびポイント 7—1間が内部熱交換器 13による熱交換、ポイント 4— 5間が膨 張弁 14による膨張、ポイント 5— 6間が蒸発器 15による蒸発をそれぞれ示しており、 ポイント 6、 7はアキュムレータ 16における同圧状態での気液分離を示している。この ように、サーマルサイフォン 17により、モリエル線図上からも効率のよい圧縮機 11の 冷却が行われることが明らかであり、ポイント 2'がポイント 3の位置にくれば、場合によ つてはガスクーラ 12の省略も可能となる。 FIG. 1 shows an equipment layout when a refrigeration system according to an embodiment of the present invention is applied to a vehicle air conditioner. In FIG. 1, the carbon dioxide refrigerant compressed and discharged by the compressor 11 is sent to the gas cooler 12 and is exchanged with the low pressure refrigerant by the high pressure refrigerant refrigerant internal heat exchanger 13 from the gas cooler 12, and then the expansion valve 14 Then, the refrigerant from the evaporator 15 passes through the accumulator 16, and is then heat-exchanged with the high-pressure side refrigerant by the internal heat exchanger 13 and sucked into the compressor 11. The thermal siphon 17 according to the present invention is provided for the compressor 11 or a part of the compressor 11 of the refrigeration system configured as described above. The thermal siphon 17 includes an evaporation unit 19 for the sealed liquid formed in the form of a jacket 18 around the compressor 11 and a condensing unit 20 positioned above. The evaporating unit 19 is disposed around the compressor 11, but the condensing unit 20 is disposed above the compressor 11. [0034] The refrigeration cycle in the refrigeration system including the thermal siphon 17 as described above can be represented by, for example, a Mollier diagram as shown in FIG. In the compression refrigeration cycle using the carbon dioxide refrigerant shown in FIG. 2, boiling cooling of the liquid sealed in the thermal siphon 17 is used for cooling the compressor 11. In Figure 2, point 1 one! The interval between '~ 2 is equivalent to the compression work by the compressor 11 (virtual component), but due to the boiling cooling by the thermal siphon 17, the compressor 11 is cooled as between the points 1' 2 'and the compressor 1 The high temperature of 1 is prevented. Between points 2 'and 3, heat is dissipated by gas cooler 12, between points 3 and 4 and between points 7 and 1, heat is exchanged by internal heat exchanger 13, between points 4 and 5 is expansion by expansion valve 14, and points 5 and 6 The intervals indicate evaporation by the evaporator 15, and points 6 and 7 indicate gas-liquid separation in the accumulator 16 under the same pressure state. Thus, it is clear that the compressor 11 is efficiently cooled by the thermal siphon 17 even on the Mollier diagram. If the point 2 ′ is at the point 3, the gas cooler Omission of 12 is also possible.

[0035] 上記サーマルサイフォン 17は、例えば図 3に示すような基本構成を有する。すなわ ち、封入液体が液相状態で流動される蒸発部 19が下部側に位置し、その上方に封 入液体が気相状態で流動され放熱により液化される凝縮部 20が配置されて!/、る。こ れらは閉回路に構成されており、蒸発部 19内部の液体が受熱気化した後、凝縮部 2 0での放熱により液化し蒸発部 19に帰還するように、閉回路で液体の移動と相変化 のサイクルを繰り返すように構成されており、蒸発部 19での気化(潜熱変化)による吸 熱により、圧縮式冷凍機の高温部が冷却されるようになっている。このように、サーマ ルサイフォン 17は、特別な外部動力を与えなくても、封入液体が循環する。  The thermal siphon 17 has a basic configuration as shown in FIG. 3, for example. In other words, the evaporation section 19 in which the sealed liquid flows in the liquid phase is located on the lower side, and the condensing section 20 in which the sealed liquid flows in the gas phase and is liquefied by heat dissipation is arranged above it! / These are configured in a closed circuit, and after the liquid inside the evaporation unit 19 has received heat and vaporized, the liquid moves in the closed circuit so that it is liquefied by heat dissipation in the condensation unit 20 and returned to the evaporation unit 19. The phase change cycle is repeated, and the high temperature part of the compression refrigerator is cooled by the endothermic heat generated by vaporization (latent heat change) in the evaporation part 19. As described above, the thermal siphon 17 circulates the sealed liquid without applying any special external power.

[0036] 図 4は、サーマルサイフォン 17に調圧室 21を設けた場合を例示している。本例で は、調圧室 21は、可撓性部材よりなり、内部にサーマルサイフォン 17内の封入液体 が流通される隔壁としての、ゴムや金属製べローズ 22と、ベローズ 22内の圧力に応 じて弹性的にストロークを変える隔壁支持部材としてのスプリング 23と、スプリング 23 のストロークの設定を調整する調整ねじ 24を備えた形態に構成されている。例えば 封入液体としての水を 100°C以下で沸騰させる場合には、ベローズ 22内圧力と大気 圧の差圧分をスプリング 23および調整ねじ 24でバランスさせればよい。水を 100°C 以上で沸騰させる場合にはスプリング 23の取付け方が逆になる。 FIG. 4 illustrates the case where the pressure regulating chamber 21 is provided in the thermal siphon 17. In this example, the pressure regulating chamber 21 is made of a flexible member, and a rubber or metal bellows 22 as a partition wall through which the sealed liquid in the thermal siphon 17 circulates, and the pressure in the bellows 22. Accordingly, a spring 23 as a partition wall supporting member that changes the stroke in response to inertia and an adjusting screw 24 for adjusting the setting of the stroke of the spring 23 are provided. For example, when boiling water as an enclosed liquid at 100 ° C. or less, the difference between the pressure inside the bellows 22 and the atmospheric pressure may be balanced by the spring 23 and the adjusting screw 24. 100 ° C water When boiling above, the installation of the spring 23 is reversed.

[0037] 図 5は、従来の圧縮機 31の一例を比較のために示したものである。この圧縮機 31 は、圧縮機構 32とそれを駆動する電動モータ 33 (例えば、 DCブラシレスモータ)が 一体に組み込まれたものからなり、電動モータ 33はインバータ 34によって制御され ている。この圧縮機 31においては、吸入冷媒 35が電動モータ 33を通して圧縮機構 32へと吸入され、それによつて圧縮機 31とともに電動モータ 33も冷却されるようにな つている。圧縮機構 32で圧縮された冷媒は、圧縮冷媒 36として吐出される。  FIG. 5 shows an example of a conventional compressor 31 for comparison. The compressor 31 is formed by integrating a compression mechanism 32 and an electric motor 33 (for example, a DC brushless motor) that drives the compression mechanism 32, and the electric motor 33 is controlled by an inverter 34. In the compressor 31, the suction refrigerant 35 is sucked into the compression mechanism 32 through the electric motor 33, thereby cooling the electric motor 33 together with the compressor 31. The refrigerant compressed by the compression mechanism 32 is discharged as the compressed refrigerant 36.

[0038] これに対し本発明を適用した、圧縮式冷凍機の冷却対象としての圧縮機は、例え ば図 6に示すように構成される。図 6は、図 1に示した圧縮機 11およびその周囲の構 成として示してある。この圧縮機 1 1は、図 5に示した圧縮機 31と同様、圧縮機構 41 が内蔵された電動モータ 42によって駆動されるものである力 吸入冷媒 43は電動モ ータ 42を通すことなく直接的に圧縮機構 41部に導入され、圧縮機構 41で圧縮され た冷媒が、圧縮冷媒 44として吐出されるようになっている。そして、この圧縮機 11に 対して、前述のジャケット 18の構造にて、サーマルサイフォン 17の蒸発部 19が配置 されており、蒸発部 19と凝縮部 20との間で、封入液体の循環が行われるように、つま り、前述したような閉回路内での液体の移動と相変化のサイクルが繰り返されるように 構成されている。また本例では、冷却のためのジャケット 18は、電動モータ 42部分を 覆うことにより電動モータ 42部分を冷却できるように配置されているとともに、電動モ ータ 42を制御するインバータ 45も冷却できるように配置されており、圧縮機 11、電動 モータ 42、インバータ 45がともに効率よく冷却されるようになっている。  On the other hand, a compressor as a cooling target of a compression refrigerator to which the present invention is applied is configured as shown in FIG. 6, for example. FIG. 6 shows the configuration of the compressor 11 shown in FIG. 1 and its surroundings. Like the compressor 31 shown in FIG. 5, the compressor 11 is driven by an electric motor 42 with a built-in compression mechanism 41. The force suction refrigerant 43 is directly passed through the electric motor 42 without passing through it. Thus, the refrigerant introduced into the compression mechanism 41 and compressed by the compression mechanism 41 is discharged as the compressed refrigerant 44. The evaporator 11 of the thermal siphon 17 is arranged with respect to the compressor 11 in the structure of the jacket 18 described above, and the sealed liquid is circulated between the evaporator 19 and the condenser 20. In other words, the liquid movement and the phase change cycle in the closed circuit as described above are repeated. In this example, the jacket 18 for cooling is arranged so that the electric motor 42 part can be cooled by covering the electric motor 42 part, and the inverter 45 that controls the electric motor 42 can also be cooled. The compressor 11, the electric motor 42, and the inverter 45 are all cooled efficiently.

[0039] このように、圧縮式冷凍機の高温部に対してサーマルサイフォンを配設することによ り、冷却が必要とされる高温部が効率よく冷却されることになり、冷凍システムの冷凍 サイクルの効率が大幅に向上されることになる。  [0039] As described above, by disposing the thermal siphon to the high temperature portion of the compression refrigerator, the high temperature portion that needs to be cooled is efficiently cooled, and the freezing of the refrigeration system is performed. The efficiency of the cycle will be greatly improved.

[0040] なお、上記実施態様は車両搭載空調装置における圧縮機部分の冷却に本発明を 適用した場合を例示した力 S、本発明は同装置のその他の部位に対しても適用可能で あり、さらに、車両塔載空調装置に限らず、他の冷凍システムにも適用可能である。 産業上の利用可能性  [0040] It should be noted that the above embodiment is a force S exemplifying the case where the present invention is applied to cooling of a compressor portion in a vehicle-mounted air conditioner, and the present invention is applicable to other parts of the apparatus, Furthermore, it is applicable not only to a vehicle-mounted air conditioner but also to other refrigeration systems. Industrial applicability

[0041] 本発明に係る冷凍システムは、とくに常温下で使用され常温レベルまでの冷却が 必要とされる用途に好適である。例えば電子機器の冷却や た圧縮式冷凍機を構成する圧縮機の冷却に好適である。 [0041] The refrigeration system according to the present invention is used at room temperature, and can be cooled to a room temperature level. Suitable for required applications. For example, it is suitable for cooling electronic devices and compressors constituting a compression refrigerator.

Claims

請求の範囲 The scope of the claims [I] 圧縮式冷凍機の高温部を冷却するために、液体が封入され該液体の蒸発部と凝 縮部とを有する閉回路に構成され、蒸発部内部の液体が受熱気化した後、凝縮部で の放熱により液化し蒸発部に帰還するように、閉回路で液体の移動と相変化のサイク ルを繰り返すサーマルサイフォンを設けたことを特徴とする冷凍システム。  [I] In order to cool the high-temperature part of the compression refrigerator, a liquid is enclosed and a closed circuit having an evaporation part and a condensation part of the liquid is formed, and after the liquid inside the evaporation part is received and vaporized, A refrigeration system provided with a thermal siphon that repeats the movement of liquid and the phase change cycle in a closed circuit so that it is liquefied by heat dissipation in the condenser and returned to the evaporator. [2] 前記サーマルサイフォンは内圧を調整することにより液体の蒸発温度が調整可能 に構成されてレ、る、請求項 1に記載の冷凍システム。  [2] The refrigeration system according to claim 1, wherein the thermal siphon is configured so that an evaporation temperature of the liquid can be adjusted by adjusting an internal pressure. [3] 前記サーマルサイフォンは、少なくとも可撓性部材よりなる隔壁と、隔壁内の圧力に 応じて弹性的にストロークを変える隔壁支持部材と、隔壁支持部材のストロークの設 定を調整する調整ねじを備えた調圧室を有する、請求項 2に記載の冷凍システム。 [3] The thermal siphon includes a partition wall made of at least a flexible member, a partition wall support member that changes its stroke in accordance with the pressure in the partition wall, and an adjustment screw that adjusts the setting of the stroke of the partition wall support member. The refrigeration system according to claim 2, further comprising a pressure regulating chamber. [4] 前記サーマルサイフォンにより冷却される圧縮式冷凍機の高温部が、圧縮機の高 温部を含む、請求項 1に記載の冷凍システム。 [4] The refrigeration system according to claim 1, wherein the high-temperature portion of the compression refrigerator cooled by the thermal siphon includes the high-temperature portion of the compressor. [5] 前記サーマルサイフォンにより冷却される圧縮式冷凍機の高温部が、圧縮機に一 体に組み込まれた電動モータを含む、請求項 1に記載の冷凍システム。 [5] The refrigeration system according to claim 1, wherein the high-temperature portion of the compression-type refrigerator cooled by the thermal siphon includes an electric motor incorporated in the compressor. [6] 前記サーマルサイフォンにより冷却される圧縮式冷凍機の高温部力 圧縮機を駆 動する電動モータを制御するインバータを含む、請求項 1に記載の冷凍システム。 6. The refrigeration system according to claim 1, further comprising an inverter that controls an electric motor that drives a high-temperature partial force compressor of the compression refrigerator cooled by the thermal siphon. [7] 前記圧縮式冷凍機の圧縮機が、その壁面を介して、前記サーマルサイフォンの蒸 発器部により冷却される、請求項 1に記載の冷凍システム。 7. The refrigeration system according to claim 1, wherein the compressor of the compression refrigerator is cooled by the evaporator unit of the thermal siphon through the wall surface. [8] 前記サーマルサイフォンに封入される液体力 水を 50%以上含む液体からなる、 請求項 1に記載の冷凍システム。 [8] The refrigeration system according to [1], comprising a liquid containing 50% or more of liquid force water enclosed in the thermal siphon. [9] 前記圧縮式冷凍機に使用される冷媒が二酸化炭素からなる、請求項 1に記載の冷 凍システム。 [9] The refrigeration system according to claim 1, wherein the refrigerant used in the compression refrigerator is made of carbon dioxide. [10] 前記サーマルサイフォンにより前記圧縮式冷凍機の圧縮機動力相当分の熱交換 が行われる、請求項 1に記載の冷凍システム。  10. The refrigeration system according to claim 1, wherein heat exchange corresponding to a compressor power of the compression refrigeration machine is performed by the thermal siphon. [I I] 車両用空調装置に用いられるものからなる、請求項 1に記載の冷凍システム。  [I I] The refrigeration system according to claim 1, wherein the refrigeration system is used for a vehicle air conditioner.
PCT/JP2007/071295 2006-11-09 2007-11-01 Refrigeration system Ceased WO2008056594A1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023020805A1 (en) * 2021-08-18 2023-02-23 Zf Cv Systems Global Gmbh Multistage, electrically drivable compressor

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20130110178A (en) 2010-10-07 2013-10-08 에이비비 리써치 리미티드 Cooling of an electric machine
DE102021134255A1 (en) * 2021-12-22 2023-06-22 OET GmbH Displacement machine based on the spiral principle

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5169255A (en) * 1974-12-12 1976-06-15 Akihiro Saito
JPS57206793A (en) * 1981-06-15 1982-12-18 Mitsubishi Heavy Ind Ltd Closed compressor
JP2000161794A (en) * 1998-11-27 2000-06-16 Calsonic Corp Air conditioner for vehicle

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5169255A (en) * 1974-12-12 1976-06-15 Akihiro Saito
JPS57206793A (en) * 1981-06-15 1982-12-18 Mitsubishi Heavy Ind Ltd Closed compressor
JP2000161794A (en) * 1998-11-27 2000-06-16 Calsonic Corp Air conditioner for vehicle

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023020805A1 (en) * 2021-08-18 2023-02-23 Zf Cv Systems Global Gmbh Multistage, electrically drivable compressor

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