JPH0875283A - Cryogenic freezing device - Google Patents
Cryogenic freezing deviceInfo
- Publication number
- JPH0875283A JPH0875283A JP21557994A JP21557994A JPH0875283A JP H0875283 A JPH0875283 A JP H0875283A JP 21557994 A JP21557994 A JP 21557994A JP 21557994 A JP21557994 A JP 21557994A JP H0875283 A JPH0875283 A JP H0875283A
- Authority
- JP
- Japan
- Prior art keywords
- cryogenic
- compressor
- gas
- ejector
- cooled
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2341/00—Details of ejectors not being used as compression device; Details of flow restrictors or expansion valves
- F25B2341/001—Ejectors not being used as compression device
- F25B2341/0011—Ejectors with the cooled primary flow at reduced or low pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2341/00—Details of ejectors not being used as compression device; Details of flow restrictors or expansion valves
- F25B2341/001—Ejectors not being used as compression device
- F25B2341/0012—Ejectors with the cooled primary flow at high pressure
Landscapes
- Separation By Low-Temperature Treatments (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、極低温冷凍装置に係
り、特に大気圧以下に減圧された極低温冷媒を生成する
に好適な極低温冷凍装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cryogenic refrigerator, and more particularly to a cryogenic refrigerator suitable for producing a cryogenic refrigerant depressurized to atmospheric pressure or less.
【0002】[0002]
【従来の技術】従来の極低温冷凍装置としては、例え
ば、特開平3−244966号公報に記載のように、冷
却段階から送られた高圧の極低温冷媒を噴射ガスとし、
被冷却体からの戻り極低温冷媒を吸入ガスとした極低温
エジェクターを有するものが知られている。2. Description of the Related Art As a conventional cryogenic refrigerator, for example, as described in JP-A-3-244966, a high-pressure cryogenic refrigerant sent from a cooling stage is used as an injection gas,
It is known to have a cryogenic ejector that uses the cryogenic refrigerant returned from the object to be cooled as an intake gas.
【0003】[0003]
【発明が解決しようとする課題】上記従来技術は、極低
温エジェクターが機構的に固定されているため運転上の
融通性が少ないという問題があった。さらに、被冷却体
の運転モードによって変動する被冷却体からの戻り極低
温冷媒流量を吸収し戻り極低温冷媒の圧力を保持するた
めには、極低温エジェクターの噴射ガス流量を熱バラン
スで必要な流量より増大せざるを得なく装置の効率が低
下するという問題があった。The above-mentioned prior art has a problem that the cryogenic ejector is mechanically fixed and therefore has little flexibility in operation. Furthermore, in order to absorb the return cryogenic refrigerant flow rate from the cooled object that varies depending on the operation mode of the cooled object and maintain the pressure of the returned cryogenic refrigerant, the injection gas flow rate of the cryogenic ejector is required to be a heat balance. There is a problem that the efficiency of the device is lowered because the flow rate must be increased.
【0004】本発明は上記従来技術の問題点を解決し、
運転操作性が良く、効率の良い極低温冷凍装置を提供す
ることを目的とする。The present invention solves the above problems of the prior art,
It is an object of the present invention to provide a cryogenic refrigeration system which has good driving operability and high efficiency.
【0005】[0005]
【課題を解決するための手段】上記目的は、被冷却体か
らの戻り極低温冷媒を昇圧するための極低温圧縮機を設
け、極低温圧縮機の吐出ガスを極低温エジェクターの吸
入ガスとすることによって達成できる。The above object is to provide a cryogenic compressor for pressurizing the cryogenic refrigerant returned from the object to be cooled, and use the discharge gas of the cryogenic compressor as the suction gas of the cryogenic ejector. Can be achieved by
【0006】[0006]
【作用】一般的に、エジェクターは狭いノズルから噴射
ガスを超音速で噴射させ、この超音速部で吸入ガスを吸
引し、ディフューザ部で圧力回復させる機構になってい
る。従って、エジェクターは外部からの仕事を要さずに
吸入ガスを昇圧できるが、吸入ガス流量が増大すると吸
入圧力が上昇するという特徴がある。In general, the ejector has a mechanism in which the injection gas is injected at a supersonic velocity from a narrow nozzle, the suction gas is sucked at the supersonic velocity portion, and the pressure is restored at the diffuser portion. Therefore, the ejector can pressurize the intake gas without requiring work from the outside, but has a feature that the intake pressure rises as the intake gas flow rate increases.
【0007】一方、圧縮機は外部から仕事を与えること
によって昇圧するもので、運転操作性は優れているが、
圧縮比が大きくなると必要な動力が増大し、実容積流量
が減少すると機器が小形化し効率が低下するという特徴
がある。On the other hand, the compressor boosts the pressure by giving work from the outside, and has excellent operability.
When the compression ratio becomes large, the required power increases, and when the actual volumetric flow rate decreases, the equipment becomes smaller and the efficiency decreases.
【0008】極低温冷凍装置、例えばヘリウム冷凍装置
では、被冷却体の運転モードにより多様な運転条件が必
要となり、被冷却体からの戻り極低温冷媒流量も大幅に
変動する。又、ヘリウム冷凍装置は、極低温(大気圧下
の液体ヘリウム温度は4.2K)のため、実容積流量が小
さくなるという特徴がある。In a cryogenic refrigerator, for example, a helium refrigerator, various operating conditions are required depending on the operation mode of the object to be cooled, and the flow rate of the cryogenic refrigerant returned from the object to be cooled also fluctuates significantly. Further, the helium refrigerating device is characterized in that the actual volumetric flow rate becomes small because it is extremely low temperature (the temperature of liquid helium under atmospheric pressure is 4.2K).
【0009】本発明は、これらの特徴を検討した結果、
大気圧下に減圧された極低温冷媒を生成するに好適な極
低温冷凍装置として、被冷却体からの戻り極低温冷媒を
運転操作性の優れた極低温圧縮機で中間圧力まで昇圧
し、冷却段階から送られた高圧極低温冷媒を噴射ガスと
する極低温エジェクターで極低温圧縮機の吐出ガスを吸
入するものであり、運転操作性の良い、高効率の極低温
冷凍装置を実現できる。The present invention, as a result of examining these characteristics,
As a cryogenic refrigerator suitable for producing cryogenic refrigerant decompressed under atmospheric pressure, the cryogenic refrigerant returned from the object to be cooled is boosted to an intermediate pressure by a cryogenic compressor with excellent operability and cooled. The discharge gas of the cryogenic compressor is sucked by the cryogenic ejector, which uses the high-pressure cryogenic refrigerant sent from the stage as the injection gas, and a highly efficient cryogenic refrigeration system with good operability can be realized.
【0010】[0010]
【実施例】以下、本発明の一実施例を図1により説明す
る。図1において、1は複数の熱交換器と複数の膨張タ
ービンを含む冷却段階、2は極低温エジェクター、3は
極低温圧縮機、4は被冷却体、5は気液分離器、6は極
低温エジェクター入口弁、7は液体ヘリウム供給弁、8
は極低温圧縮機出口弁、9は極低温圧縮機バイパス弁、
10は極低温圧縮機バイパスラインである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. In FIG. 1, 1 is a cooling stage including a plurality of heat exchangers and a plurality of expansion turbines, 2 is a cryogenic ejector, 3 is a cryogenic compressor, 4 is a cooled object, 5 is a gas-liquid separator, and 6 is a pole. Low temperature ejector inlet valve, 7 liquid helium supply valve, 8
Is a cryogenic compressor outlet valve, 9 is a cryogenic compressor bypass valve,
Reference numeral 10 is a cryogenic compressor bypass line.
【0011】次に、以上のように構成された本発明の実
施例の動作を説明する。複数の熱交換器と複数の膨張タ
ービンを含む冷却段階1から供給された高圧の極低温冷
媒は、極低温エジェクター入口弁6を通り極低温エジェ
クター2の噴射ガスとなり、極低温エジェクター2の中
で吸入ガスと混合し、気液混相状態となって気液分離器
5に供給される。気液分離器5で気液分離された極低温
ヘリウムガスは冷却段階1に戻り、液体ヘリウムは液体
ヘリウム供給弁7を通り被冷却体4に供給される。被冷
却体4を冷却しガス化した極低温ヘリウムガスは、極低
温圧縮機3で中間圧力まで昇圧され、極低温圧縮機出口
弁8を通り極低温エジェクター2の吸入ガスとなる。Next, the operation of the embodiment of the present invention constructed as above will be described. The high-pressure cryogenic refrigerant supplied from the cooling stage 1 including a plurality of heat exchangers and a plurality of expansion turbines passes through the cryogenic ejector inlet valve 6 to become a jet gas of the cryogenic ejector 2, and in the cryogenic ejector 2. It is mixed with the suction gas, and is brought into a gas-liquid mixed state, and is supplied to the gas-liquid separator 5. The cryogenic helium gas gas-liquid separated by the gas-liquid separator 5 returns to the cooling stage 1, and liquid helium is supplied to the cooled object 4 through the liquid helium supply valve 7. The cryogenic helium gas obtained by cooling and cooling the cooled object 4 is boosted to an intermediate pressure by the cryogenic compressor 3, passes through the cryogenic compressor outlet valve 8 and becomes the suction gas of the cryogenic ejector 2.
【0012】極低温エジェクター入口弁6は、極低温冷
凍装置の種々の運転条件に合わせ極低温エジェクター2
の噴射ガス流量を調整するために設けられている。液体
ヘリウム供給弁7は、被冷却体4の熱負荷に合わせ供給
する液体ヘリウムを制御するために設けられ、減圧弁も
兼ねている。極低温圧縮機出口弁8は、極低温圧縮機3
が停止中にラインを閉止するために設けられ、極低温圧
縮機バイパス弁9及び極低温圧縮機バイパスライン10
は、極低温圧縮機3を使用しない運転のために設けられ
ている。The cryogenic ejector inlet valve 6 is adapted to the cryogenic ejector 2 in accordance with various operating conditions of the cryogenic refrigeration system.
It is provided for adjusting the flow rate of the injection gas of. The liquid helium supply valve 7 is provided to control the liquid helium to be supplied in accordance with the heat load of the object to be cooled 4, and also serves as a pressure reducing valve. The cryogenic compressor outlet valve 8 is used for the cryogenic compressor 3
Is provided for closing the line during stoppage, and the cryogenic compressor bypass valve 9 and the cryogenic compressor bypass line 10 are provided.
Are provided for operation without using the cryogenic compressor 3.
【0013】極低温圧縮機3は、被冷却体4の運転モー
ドによって変動する極低温ヘリウムガス流量に対応し、
図示しない制御手段によって極低温ヘリウムガスの圧力
を所定の設定値に保持するように容量制御(例えば、回
転数制御)される。The cryogenic compressor 3 corresponds to the cryogenic helium gas flow rate which varies depending on the operation mode of the object to be cooled 4,
The capacity of the cryogenic helium gas is controlled by a control means (not shown) so as to maintain the pressure of the cryogenic helium gas at a predetermined set value (for example, rotation speed control).
【0014】以上、詳細に説明したように、本実施例に
よれば運転操作性に優れた極低温圧縮機で中間圧力まで
昇温し、冷却段階から送られる高圧の極低温冷媒を噴射
ガスとする極低温エジェクターの吸入ガスとするため、
運転操作性が良く、高効率の極低温冷凍装置を実現でき
るという効果がある。As described above in detail, according to the present embodiment, the cryogenic compressor which is excellent in driving operability raises the temperature to the intermediate pressure, and the high pressure cryogenic refrigerant sent from the cooling stage is used as the injection gas. In order to make it as the inhaled gas of the cryogenic ejector,
There is an effect that it is possible to realize a highly efficient cryogenic refrigerating device having good driving operability.
【0015】[0015]
【発明の効果】本発明によれば、冷却段階から送られる
高圧の極低温冷媒を噴射ガスとする極低温エジェクター
を有し、被冷却体からの戻り極低温冷媒を中間圧力まで
昇圧する極低温圧縮機を有し、極低温圧縮機の吐出ガス
を極低温エジェクターの吸入ガスとすることにより、被
冷却体の多様な熱負荷条件を運転操作性の優れた極低温
圧縮機で吸入し、外部動力を要しない極低温エジェクタ
ーで極低温圧縮機の吐出ガスを吸入・昇圧するため、運
転操作性が良く、高効率の極低温冷凍装置を実現できる
という効果がある。EFFECTS OF THE INVENTION According to the present invention, a cryogenic temperature is provided which has a cryogenic ejector which uses a high-pressure cryogenic refrigerant sent from the cooling stage as an injection gas, and which boosts the cryogenic refrigerant returned from an object to be cooled to an intermediate pressure. By having a compressor and using the discharge gas of the cryogenic compressor as the suction gas of the cryogenic ejector, various heat load conditions of the object to be cooled are sucked in by the cryogenic compressor with excellent driving operability, and external Since the cryogenic ejector, which does not require power, sucks in and boosts the gas discharged from the cryogenic compressor, there is an effect that a highly efficient cryogenic refrigeration system can be realized with good operability.
【図1】本発明の一実施例を示す系統図である。FIG. 1 is a system diagram showing an embodiment of the present invention.
1…冷却段階、2…極低温エジェクター、3…極低温圧
縮機、4…被冷却体、5…気液分離器。1 ... Cooling stage, 2 ... Cryogenic ejector, 3 ... Cryogenic compressor, 4 ... Cooled object, 5 ... Gas-liquid separator.
Claims (6)
するため複数の熱交換器と複数の膨張タービンを含む冷
却段階と、極低温冷媒で冷却される被冷却体を有する極
低温冷凍装置において、上記冷却段階から送られた高圧
の極低温冷媒を噴射ガスとする極低温エジェクターと、
上記被冷却体からの戻り極低温冷媒を昇圧するたための
極低温圧縮機とを有し、上記極低温圧縮機の吐出ガスを
上記極低温エジェクターの吸入ガスとしたことを特徴と
する極低温冷凍装置。1. A cryogenic refrigeration system having a cooling stage including a plurality of heat exchangers and a plurality of expansion turbines for cooling a high pressure gas stream to near a liquefied gas temperature, and an object to be cooled which is cooled with a cryogenic refrigerant. In, a cryogenic ejector that uses the high-pressure cryogenic refrigerant sent from the cooling stage as an injection gas,
A cryogenic refrigerator having a cryogenic compressor for pressurizing a cryogenic refrigerant returned from the object to be cooled, wherein a discharge gas of the cryogenic compressor is a suction gas of the cryogenic ejector. apparatus.
極低温圧縮機としたことを特徴とする極低温冷凍装置。2. A cryogenic refrigerating apparatus, wherein the cryogenic compressor according to claim 1 is a turbo cryogenic compressor.
極低温圧縮機のバイパスラインを設けたことを特徴とす
る極低温冷凍装置。3. The cryogenic refrigerating apparatus according to claim 1,
A cryogenic refrigerator equipped with a bypass line for a cryogenic compressor.
極低温圧縮機の入口圧力を極低温圧縮機の容量制御によ
り所定の設定値に保持する制御手段を有することを特徴
とする極低温冷凍装置。4. The cryogenic refrigerating apparatus according to claim 1,
A cryogenic refrigeration system comprising a control means for holding the inlet pressure of the cryogenic compressor at a predetermined set value by controlling the capacity of the cryogenic compressor.
る極低温圧縮機、及び極低温エジェクター。5. A cryogenic compressor and a cryogenic ejector used in the cryogenic refrigerating apparatus according to claim 1.
る被冷却体。6. An object to be cooled, which is cooled by the cryogenic refrigerating apparatus according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21557994A JPH0875283A (en) | 1994-09-09 | 1994-09-09 | Cryogenic freezing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21557994A JPH0875283A (en) | 1994-09-09 | 1994-09-09 | Cryogenic freezing device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0875283A true JPH0875283A (en) | 1996-03-19 |
Family
ID=16674781
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21557994A Pending JPH0875283A (en) | 1994-09-09 | 1994-09-09 | Cryogenic freezing device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0875283A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102620461A (en) * | 2012-04-19 | 2012-08-01 | 浙江大学宁波理工学院 | Auto-cascade jet type refrigerator |
JP2013127353A (en) * | 2011-11-18 | 2013-06-27 | Sumitomo Heavy Ind Ltd | Freezer |
WO2021012725A1 (en) * | 2019-07-22 | 2021-01-28 | 北京市京科伦冷冻设备有限公司 | Carbon dioxide refrigerating system and refrigerating method thereof |
CN112696843A (en) * | 2021-01-08 | 2021-04-23 | 西北工业大学 | Jet type refrigerating device for compressing liquid refrigerant |
-
1994
- 1994-09-09 JP JP21557994A patent/JPH0875283A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013127353A (en) * | 2011-11-18 | 2013-06-27 | Sumitomo Heavy Ind Ltd | Freezer |
CN102620461A (en) * | 2012-04-19 | 2012-08-01 | 浙江大学宁波理工学院 | Auto-cascade jet type refrigerator |
WO2021012725A1 (en) * | 2019-07-22 | 2021-01-28 | 北京市京科伦冷冻设备有限公司 | Carbon dioxide refrigerating system and refrigerating method thereof |
CN112696843A (en) * | 2021-01-08 | 2021-04-23 | 西北工业大学 | Jet type refrigerating device for compressing liquid refrigerant |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20220113065A1 (en) | Ejector Cycle | |
CN1470821B (en) | Injector with throttle controllable nozzle and injection circulation using same | |
CN107532828B (en) | Ejector refrigeration circuit | |
US8776539B2 (en) | Ejector-type refrigeration cycle and refrigeration device using the same | |
JPH0814681A (en) | Refrigerator using high-pressure primary closed refrigeration loop and secondary refrigeration loop | |
EP2728278A1 (en) | Refrigeration cycle device and air conditioner | |
JP2003329313A (en) | Vapor compression type refrigerating machine | |
US20200292219A1 (en) | Ejector and refrigeration system | |
JP2004309093A (en) | Heat pump type hot water supply apparatus with cooling function | |
JP2838917B2 (en) | Refrigeration cycle | |
JPS60159561A (en) | Two-step compression refrigerator | |
JP2001090684A (en) | Screw compressor and freezing device | |
JPH0875283A (en) | Cryogenic freezing device | |
JP2002349977A (en) | Heat pump cycle | |
JP2003097868A (en) | Ejector cycle | |
JPH0875284A (en) | Cryogenic freezing device | |
JPH1137577A (en) | Nozzle device | |
KR20020028521A (en) | Variable capacity ejector | |
WO2020113332A1 (en) | System and method of mechanical compression refrigeration based on two-phase ejector | |
JPH0626718A (en) | Freezing cycle | |
JPH10292948A (en) | Refrigerator | |
JPH06101919A (en) | Cryogenic freezing apparatus | |
JPS59225259A (en) | Refrigerator | |
JPS63306361A (en) | Cold accumulator type refrigerator | |
JP2004325013A (en) | Refrigerating cycle device |