JPH03217763A - Cryogenic refrigerator - Google Patents

Cryogenic refrigerator

Info

Publication number
JPH03217763A
JPH03217763A JP1292290A JP1292290A JPH03217763A JP H03217763 A JPH03217763 A JP H03217763A JP 1292290 A JP1292290 A JP 1292290A JP 1292290 A JP1292290 A JP 1292290A JP H03217763 A JPH03217763 A JP H03217763A
Authority
JP
Japan
Prior art keywords
compressor
pressure
valve
pipe
tube
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
Application number
JP1292290A
Other languages
Japanese (ja)
Inventor
Tokuji Nishijo
西場 徳二
Shigeru Murayama
茂 村山
Kazuo Nomura
野村 和雄
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP1292290A priority Critical patent/JPH03217763A/en
Publication of JPH03217763A publication Critical patent/JPH03217763A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To hold a pressure difference between the high pressures side and the low pressure side of a compressor constant by regulating the opening of a motor-driven expansion valve provided in a bypass tube for maintaining the pressure difference constant by returning fluid from the high pressure side to the low pressure side of the compressor by a controller which is operated by detecting pressures of discharge and suction tubes of the compressor. CONSTITUTION:A motor-driven expansion valve 19 provided in a bypass tube 18 connected to a high pressure tube 7 between an oil separator 3 and an adsorber 4 and a low pressure tube 9 on the inlet side of an accumulator 6 is controlled in its opening by a controller 23 which calculates the difference of the pressures detected by a first pressure sensor 21 mounted in the tube 7 on the outlet side of a compressor 1 and detected by a second pressure sensor 22 provided in the tube 9, and a pressure difference between the fluid sucked to the compressor 1 and the discharged fluid is held constant. The valve 19 rapidly sets the pressure difference between the tubes 7 and 9 connected to the compressor 1 to zero by fully opening the valve when the compressor 1 is stopped. Further, the valve 19 can be optimally regulated at the pressure difference between the discharge side and the suction side of the compressor 1 under the control of the valve opening by the pressures detected by the sensors 21, 22.

Description

【発明の詳細な説明】 (イ》産業上の利用分野 この発明は圧縮機の高圧側と低圧側との圧力差を一定に
保持する極低温用冷凍装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (A) Industrial Application Field This invention relates to a cryogenic refrigeration system that maintains a constant pressure difference between a high pressure side and a low pressure side of a compressor.

(口)従来の技術 従来の極低温用冷凍装置は例えば実公昭52一9638
号公報に示されているように構成されている。ここで、
この公報を参考に従来例を説明する。第4図において、
50.51は圧縮機及び圧力調整弁、52 .53は圧
縮機50の電源に連動する自動弁、54はフィルタから
なる高圧機器、55は極低温膨張機、56.57は復帰
路及びガスホルダである。
(Example) Conventional technology A conventional cryogenic refrigeration system is, for example,
The structure is as shown in the publication. here,
A conventional example will be explained with reference to this publication. In Figure 4,
50.51 is a compressor and pressure regulating valve; 52. 53 is an automatic valve linked to the power supply of the compressor 50, 54 is a high-pressure device consisting of a filter, 55 is a cryogenic expander, and 56 and 57 are a return path and a gas holder.

この構造の極低温用冷凍装置では圧縮機50で圧縮され
た流体例えばヘリウムガスを圧力調整弁51で復帰路5
6に戻して極低温膨張機55に供給する流体の圧力を調
整した後、自動弁52、高圧機器54及び自動弁53を
通って極低温膨張機55で寒冷を作るとともに、停止時
に自動弁52,53を閉じて高圧機器54内の流体を高
圧状態でこの高圧機器内に封じ込めるようにしている。
In the cryogenic refrigeration system with this structure, fluid compressed by the compressor 50, for example, helium gas, is transferred to the return path 5 through the pressure regulating valve 51.
6 to adjust the pressure of the fluid supplied to the cryogenic expander 55, and then pass through the automatic valve 52, high-pressure equipment 54, and automatic valve 53 to generate cold air in the cryogenic expander 55, and when stopped, the automatic valve 52 , 53 are closed to confine the fluid within the high-pressure device 54 in a high-pressure state within this high-pressure device.

(ハ)発明が解決しようとする課題 しかしながら、圧力調整弁51は前後の高圧圧力と低圧
圧力との圧力差で作動しているため、圧縮機50の吸込
側と吐出側との実際の圧力に応じて作動することがなく
、前記圧縮機5oの実際の運転の圧力に応じられず、冷
凍能力が安定しなくなる間潤があった。
(C) Problems to be Solved by the Invention However, since the pressure regulating valve 51 operates based on the pressure difference between the high pressure and the low pressure at the front and rear, the actual pressure between the suction side and the discharge side of the compressor 50 may vary. The compressor 5o did not operate according to the actual operating pressure, and there was a period when the refrigerating capacity became unstable.

この発明は上記の問題を解決するもので、圧縮機の高圧
側と低圧側との圧力差を一定に保持できるようにする極
低温用冷凍装置を提供することを目的としたものである
This invention solves the above-mentioned problem, and aims to provide a cryogenic refrigeration system that can maintain a constant pressure difference between the high pressure side and the low pressure side of the compressor.

《二》課題を解決するための手段 この発明は圧縮機、主熱交換器、オイルセパレータ、ア
ドソーバ及び極低温用膨張機を配管接続し、前記圧縮機
の吸込側とオイルセバレー夕の出口側との間にバイパス
管を設けた極低温用冷凍装置において、前記バイパス管
に電動膨張弁を設け、かつ、この電動膨張弁の開度を制
御する制御装置を、圧縮機の吐出管及び吸込管との圧力
を検出するセンサと、このセンサからの出力を演算する
コントローラとで構成したものである。
[2] Means for Solving the Problems This invention connects a compressor, a main heat exchanger, an oil separator, an adsorber, and a cryogenic expander with piping, and connects the suction side of the compressor and the outlet side of the oil separator. In a cryogenic refrigeration system in which a bypass pipe is provided between the bypass pipe and the bypass pipe, an electric expansion valve is provided in the bypass pipe, and a control device for controlling the opening degree of the electric expansion valve is connected to the discharge pipe and the suction pipe of the compressor. It is composed of a sensor that detects the pressure of the sensor, and a controller that calculates the output from this sensor.

(ホ)作用 この発明は上記のように構成したことにより、圧縮機の
吐出管と吸込管との圧力を検出するセンサからの出力を
演算する制御装置からの信号で電動膨張弁の開度を調整
し、前記圧縮機の高圧圧力と低圧圧力との圧力差を一定
に保持して最適な運転が行えるようにしたものである。
(E) Function This invention is configured as described above, so that the opening degree of the electric expansion valve is controlled by a signal from a control device that calculates the output from a sensor that detects the pressure between the discharge pipe and suction pipe of the compressor. The pressure difference between the high pressure and the low pressure of the compressor is maintained constant to enable optimum operation.

(へ)実施例 以下この発明を第1図及び第2図に示す実施例に基いて
説明する。
(f) Examples The present invention will be explained below based on the examples shown in FIGS. 1 and 2.

1はヘリウムガス等の流体を圧縮する圧縮機、2は主熱
交換器、3はオイルセパレータ、4はアドソーバ、5は
極低温膨張機、6はアキュームレータである。圧縮機1
と極低温膨張機5との間には、オイルセパレータ3とア
ドソーバ4とを介して高圧管7が接続されている。そし
て、極低温膨張機5の入口側の高圧管7には吸気弁8が
設けられている。極低温膨張機5と圧縮機1との間には
、アキュームレータ6を介して低圧管9が接続されてい
る。極低温膨張機5の出口側の低圧管9には排気弁10
が設けられている。圧縮機1は底部にオイルを貯溜した
密閉容器11と、この容器内に収納された圧縮要素(図
示せず)とで構成されている。12は密閉容器11内の
オイルを圧縮要素内に供給するオイル供給管で、このオ
イル供給管にはオイルを冷郎するオイル冷却器13が設
けられてル)る。14は補助熱交換器で、この補助熱交
換器は圧縮要素で圧縮された流体を密閉容器1外に吐出
して冷却した後、再度密閉容器1内に導入させるように
している。15はオイル戻し管で、このオイル戻し管は
オイルセバレータ3とアキュームレータ6の出口側との
間に接続されている。16.17はオイル供給管12と
才イル戻し管15とに夫々設けられた減圧用のキャピラ
リーチュープである。
1 is a compressor that compresses fluid such as helium gas, 2 is a main heat exchanger, 3 is an oil separator, 4 is an adsorber, 5 is a cryogenic expander, and 6 is an accumulator. Compressor 1
A high pressure pipe 7 is connected between the and the cryogenic expander 5 via an oil separator 3 and an adsorber 4. An intake valve 8 is provided in the high pressure pipe 7 on the inlet side of the cryogenic expander 5. A low pressure pipe 9 is connected between the cryogenic expander 5 and the compressor 1 via an accumulator 6. An exhaust valve 10 is installed in the low pressure pipe 9 on the outlet side of the cryogenic expander 5.
is provided. The compressor 1 is comprised of a closed container 11 in which oil is stored at the bottom, and a compression element (not shown) housed within this container. Reference numeral 12 denotes an oil supply pipe for supplying the oil in the closed container 11 into the compression element, and this oil supply pipe is provided with an oil cooler 13 for cooling the oil. Reference numeral 14 denotes an auxiliary heat exchanger, and this auxiliary heat exchanger discharges the fluid compressed by the compression element outside the closed container 1 to cool it, and then introduces it into the closed container 1 again. 15 is an oil return pipe, and this oil return pipe is connected between the oil separator 3 and the outlet side of the accumulator 6. Reference numerals 16 and 17 are capillary tubes for reducing pressure provided in the oil supply pipe 12 and the oil return pipe 15, respectively.

18はオイルセパレータ3とアドソーバ4との間の高圧
管7と、アキュームレータ6の入口側の低圧管9とに接
続されたバイパス管で、このバイパス管には電動膨張弁
19が設けられている。20は電動膨張弁19の開度を
制御する制御装置で、この制御装置は圧縮機と主熱交換
器2との間の高圧管7に取付けられた第1圧カセンサ2
1と、排気弁10とアキュームレータ6との間の低圧管
9に取付けられた第2圧カセンサ22と、第1・第2圧
カセンサ21,22からの出力を演算するフントローラ
23とで構成されている。
A bypass pipe 18 is connected to the high pressure pipe 7 between the oil separator 3 and the adsorber 4 and the low pressure pipe 9 on the inlet side of the accumulator 6, and this bypass pipe is provided with an electric expansion valve 19. Reference numeral 20 denotes a control device that controls the opening degree of the electric expansion valve 19, and this control device includes a first pressure sensor 2 attached to the high pressure pipe 7 between the compressor and the main heat exchanger 2.
1, a second pressure sensor 22 attached to the low pressure pipe 9 between the exhaust valve 10 and the accumulator 6, and a mount roller 23 that calculates the outputs from the first and second pressure sensors 21 and 22. There is.

このように構成された極低温用冷凍装置において、圧縮
機1で圧縮された流体は補助熱交換器14で冷却された
後、再度密閉容器11内に流入し、高圧管7から主熱交
換器2に吐出される。この主熱交換器で冷却された流体
はオイルセパレータ3で内部に含まれているオイルの大
部分を分離されている。この才イルセパレー夕から流出
した流体はアドソーバ4を通過する際に、オイルセバレ
ータ3で分離しきれなかった油粒子をアドソーバ4で吸
着させてオイルが十分に除去されるようにしている。ア
ドソーバ3を出た流体は吸気弁8゛が開放しているとき
、極低温膨張機5に入って膨張して寒冷を発生している
。また、寒冷を発生した流体は排気弁10が開放するこ
とにより、極低温膨張機5内で熱交換して外気温度と略
同等になってアキュームレータ6を介して圧縮機1に帰
還するようにしている。吸気弁8と排気弁10とは交互
に開閉して流体を極低温膨張機5に高圧管7側から流入
して低圧管9側へ流出させるようにしている。
In the cryogenic refrigeration system configured as described above, the fluid compressed by the compressor 1 is cooled by the auxiliary heat exchanger 14, and then flows into the closed container 11 again, and is transferred from the high pressure pipe 7 to the main heat exchanger. 2. The fluid cooled by this main heat exchanger is separated from most of the oil contained therein by an oil separator 3. When the fluid flowing out from the oil separator passes through the adsorber 4, oil particles that cannot be separated by the oil separator 3 are adsorbed by the adsorber 4, so that the oil is sufficiently removed. When the intake valve 8' is open, the fluid leaving the adsorber 3 enters the cryogenic expander 5 and expands to generate cold. Furthermore, when the exhaust valve 10 is opened, the cold fluid exchanges heat within the cryogenic expander 5 and returns to the compressor 1 via the accumulator 6 after becoming approximately equal to the outside air temperature. There is. The intake valve 8 and the exhaust valve 10 are alternately opened and closed to allow fluid to flow into the cryogenic expander 5 from the high pressure pipe 7 side and flow out to the low pressure pipe 9 side.

密閉容器11内の底部に貯溜されたオイルはオイル供給
管12で外部に流出されてオイル冷却器13により冷却
され、減圧用のキャピラリチュープ16で減圧されてア
キュームレータ6の出口側に戻して流体に混合するよう
にしている。また、オイルセパレータ3で分離されたオ
イルはオイル戻し管15から減圧用のキャビラリチュー
ブ17で減圧されてアキュームレータ6の出口側に戻し
て流体に混合するようにしている。そして、圧縮機1に
戻ったオイルはアキュームレータ6からこの圧縮機に供
給される流体の圧縮による温度上昇を抑えられるように
している。
The oil stored at the bottom of the closed container 11 flows out through an oil supply pipe 12, is cooled by an oil cooler 13, is depressurized by a decompression capillary tube 16, and is returned to the outlet side of the accumulator 6 to become a fluid. I try to mix it up. Further, the oil separated by the oil separator 3 is depressurized from the oil return pipe 15 by a depressurizing cabillary tube 17 and returned to the outlet side of the accumulator 6 to be mixed with the fluid. The temperature of the oil returned to the compressor 1 is suppressed from increasing due to compression of the fluid supplied from the accumulator 6 to the compressor.

オイルセパレータ3とアドソーバ4との間の高圧管7と
、アキュームレータ6の入口側の低圧管9とに接続され
たバイパス管18に設けられた電動膨張弁19は圧縮機
1の出口側の高圧管7に取付けた第1圧カセンサ21と
低圧管9に取付けた第2圧カセンサ22とで検出された
圧力の差をコントローラ23で演算して弁開度を制御す
ることにより、圧縮機1に吸込まれる流体と吐出される
流体との圧力差を一定に保持できるようにしている。ま
た、電動膨張弁19は圧縮機1の停止時に弁開度を全開
にすることにより、圧縮機1に接続された高圧管7内と
低圧管9内との圧力差を速やかにゼロにすることができ
るようにしている。
An electric expansion valve 19 installed in a bypass pipe 18 connected to a high-pressure pipe 7 between the oil separator 3 and the adsorber 4 and a low-pressure pipe 9 on the inlet side of the accumulator 6 is connected to the high-pressure pipe 7 on the outlet side of the compressor 1. The controller 23 calculates the difference between the pressures detected by the first pressure sensor 21 attached to the pipe 7 and the second pressure sensor 22 attached to the low pressure pipe 9 and controls the valve opening. This makes it possible to maintain a constant pressure difference between the fluid injected and the fluid discharged. In addition, the electric expansion valve 19 can quickly reduce the pressure difference between the high pressure pipe 7 and the low pressure pipe 9 connected to the compressor 1 to zero by fully opening the valve when the compressor 1 is stopped. We are making it possible to do so.

きらに、電動膨張弁19は第1・第2圧カセンサ21,
22で検出された圧力で弁開度を制御することにより、
バイパス管18に到達する流体の圧力損失を考慮する必
要がなく圧縮機1の吐出側と吸込側との圧力差を最適に
調整することができるようにしている。
Additionally, the electric expansion valve 19 has first and second pressure sensors 21,
By controlling the valve opening degree with the pressure detected at 22,
There is no need to consider the pressure loss of the fluid reaching the bypass pipe 18, and the pressure difference between the discharge side and the suction side of the compressor 1 can be adjusted optimally.

この発明は第1・第2圧カセンサ21 ,22で圧縮機
1の吸込側の圧力と吐出側の圧力とを検出してバイパス
管18に設けた電動膨張弁19の弁開度を制御すること
により、圧縮機1で圧縮諮れる流体の高低圧力差を一定
にできるようにしたものである。
This invention detects the pressure on the suction side and the pressure on the discharge side of the compressor 1 using first and second pressure sensors 21 and 22 to control the valve opening degree of the electric expansion valve 19 provided in the bypass pipe 18. This makes it possible to keep the pressure difference between the high and low pressures of the fluid compressed by the compressor 1 constant.

尚、上記説明においては、高圧管7と低圧管9とに夫々
圧カセンサ21,22を取付けて説明したが、第3図に
示すように圧カセンサの代わりに高圧管7と低圧管9と
の間に差圧センサ24を設けても同様な効果を有するこ
とは言うまでもない。
In the above explanation, the pressure sensors 21 and 22 were attached to the high pressure pipe 7 and the low pressure pipe 9, respectively, but as shown in FIG. Needless to say, the same effect can be obtained even if the differential pressure sensor 24 is provided in between.

(ト)発明の効果 以上のようにこの発明によれば、圧縮機の高圧側から低
圧側へ流体を戻して高圧側と低圧側との圧力差を一定に
するバイパス管に設けた電動膨張弁の開度を、圧縮機の
吐出管と吸込管との圧力を検出して作動させる制御装置
で調整するのであるから、圧力調整を流体の圧力損失を
考慮する必要がなく行うことができ、圧縮機の高圧側と
低圧側との圧力差を一定にできるものである。しかも、
この発明は制御装置の圧力設定を任意に変えられるので
、運転中に設定を変更することができるものである。
(G) Effects of the Invention As described above, according to the present invention, an electric expansion valve is installed in a bypass pipe to return fluid from the high pressure side to the low pressure side of the compressor to keep the pressure difference between the high pressure side and the low pressure side constant. Since the opening degree of the compressor is adjusted by a control device that detects the pressure between the discharge pipe and suction pipe of the compressor and operates the compressor, the pressure can be adjusted without having to consider the pressure loss of the fluid. This allows the pressure difference between the high pressure side and low pressure side of the machine to be constant. Moreover,
In this invention, since the pressure setting of the control device can be changed arbitrarily, the setting can be changed during operation.

【図面の簡単な説明】[Brief explanation of drawings]

第1図はこの発明の一実施例を示す極低温用冷凍機の冷
却回路図、第2図は同じく圧縮機の圧力制御装置を示す
要部冷却回路図、第3図は同じく他の実施例を示す極低
温用冷凍機の冷却回路図、第4図は従来例を示す冷却回
路図である。 1・・・圧縮機、 2・・・主熱交換器、 3・・・オ
イルセパレータ、  4・・・アドソーバ、  7・・
・高圧管、9・・・低圧管、  18・・・バイパス管
、  19・・・電動膨張弁、 20・・・制御装置、
 21・・・第1圧カセンサ、 22・・・第2圧カセ
ンサ、  23・・・コントローラ、  24・・・差
圧センサ。
Fig. 1 is a cooling circuit diagram of a cryogenic refrigerator showing one embodiment of the present invention, Fig. 2 is a main part cooling circuit diagram showing a compressor pressure control device, and Fig. 3 is a similar diagram of another embodiment. FIG. 4 is a cooling circuit diagram of a conventional example. 1... Compressor, 2... Main heat exchanger, 3... Oil separator, 4... Adsorber, 7...
- High pressure pipe, 9... Low pressure pipe, 18... Bypass pipe, 19... Electric expansion valve, 20... Control device,
21... First pressure sensor, 22... Second pressure sensor, 23... Controller, 24... Differential pressure sensor.

Claims (1)

【特許請求の範囲】[Claims] 1、圧縮機、主熱交換器、オイルセパレータ、アドソー
バ及び極低温用膨張機を配管接続し、前記圧縮機の吸込
側とオイルセパレータの出口側との間にバイパス管を設
けた極低温用冷凍装置において、前記バイパス管には電
動膨張弁が設けられ、かつ、この電動膨張弁の開度を制
御する制御装置を、圧縮機の吐出管及び吸込管との圧力
を検出するセンサと、このセンサからの出力を演算する
コントローラとで構成したことを特徴とする極低温用冷
凍装置。
1. A cryogenic refrigeration system in which a compressor, a main heat exchanger, an oil separator, an adsorber, and a cryogenic expander are connected via piping, and a bypass pipe is provided between the suction side of the compressor and the outlet side of the oil separator. In the apparatus, the bypass pipe is provided with an electric expansion valve, and a control device that controls the opening degree of the electric expansion valve is connected to a sensor that detects the pressure between the discharge pipe and the suction pipe of the compressor, and this sensor. A cryogenic refrigeration device characterized by comprising a controller that calculates an output from the cryogenic refrigeration device.
JP1292290A 1990-01-22 1990-01-22 Cryogenic refrigerator Pending JPH03217763A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1292290A JPH03217763A (en) 1990-01-22 1990-01-22 Cryogenic refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1292290A JPH03217763A (en) 1990-01-22 1990-01-22 Cryogenic refrigerator

Publications (1)

Publication Number Publication Date
JPH03217763A true JPH03217763A (en) 1991-09-25

Family

ID=11818830

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1292290A Pending JPH03217763A (en) 1990-01-22 1990-01-22 Cryogenic refrigerator

Country Status (1)

Country Link
JP (1) JPH03217763A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004085048A (en) * 2002-08-26 2004-03-18 Sumitomo Heavy Ind Ltd Cryogenic freezing device and its operation method
US20220279684A1 (en) * 2019-07-09 2022-09-01 Nec Corporation Cooling system, surge generation prevention device, surge generation prevention method, and surge generation prevention program

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004085048A (en) * 2002-08-26 2004-03-18 Sumitomo Heavy Ind Ltd Cryogenic freezing device and its operation method
US20220279684A1 (en) * 2019-07-09 2022-09-01 Nec Corporation Cooling system, surge generation prevention device, surge generation prevention method, and surge generation prevention program

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