JPH08313085A - Method and apparatus for controlling pressure equalization of cryogenic refrigerating machine - Google Patents

Method and apparatus for controlling pressure equalization of cryogenic refrigerating machine

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Publication number
JPH08313085A
JPH08313085A JP12342495A JP12342495A JPH08313085A JP H08313085 A JPH08313085 A JP H08313085A JP 12342495 A JP12342495 A JP 12342495A JP 12342495 A JP12342495 A JP 12342495A JP H08313085 A JPH08313085 A JP H08313085A
Authority
JP
Japan
Prior art keywords
pressure
compressors
refrigerant
valve
compressor
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.)
Granted
Application number
JP12342495A
Other languages
Japanese (ja)
Other versions
JP2725631B2 (en
Inventor
Keiji Tomioka
計次 富岡
Shoichi Tanetani
昭一 種谷
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries 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 Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP12342495A priority Critical patent/JP2725631B2/en
Publication of JPH08313085A publication Critical patent/JPH08313085A/en
Application granted granted Critical
Publication of JP2725631B2 publication Critical patent/JP2725631B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE: To lower the equalizing pressure of a refrigerant circuit by holding a refrigerant circuit between a compressor and expansion means in an open state for a predetermined time at the time of stopping the compressor, and feeding the gas refrigerant of the compressor to the expansion means side to reduce the gas refrigerant quantity at the compressor side. CONSTITUTION: When compressors 4, 8 are stopped due to the stop of a refrigerating machine R, switching means 54 is controlled to be switched by control means 61. The means 54 is held in an open state until a predetermined time is elapsed from the stops of the compressors 4, 8. Thus, the compressors 4, 8 are held to communicate with expansion means 41, the gas refrigerant in the high-pressure tube 15 of a refrigerant circuit 53 due to the stops of the compressors 4, 8 flows to the means 41 side by the differential pressure between the compressors 4, 8 and the means 41, and hence the gas refrigerant amount of the side of the compressors 4, 8 in the circuit 53 is reduced. In this manner, the equalizing pressure of the circuit 53 can be lowered.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、圧縮機で圧縮された
ヘリウムガス等のガス冷媒を膨張機で膨張させて極低温
レベルの寒冷を発生させるようにした極低温冷凍機にお
いて、その圧縮機の停止時の冷媒回路の圧力を均圧に制
御するようにした均圧制御装置及び均圧制御方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cryogenic refrigerator in which a gas refrigerant such as helium gas compressed by a compressor is expanded by an expander to generate cryogenic cold. TECHNICAL FIELD The present invention relates to a pressure equalizing control device and a pressure equalizing control method for controlling the pressure of a refrigerant circuit at the time of stop of pressure equalization.

【0002】[0002]

【従来の技術】一般に、超電導現象を利用する超電導体
においては、その温度を臨界温度以下に冷却保持するた
めにタンク内に貯溜した液体ヘリウムを用いることが行
われているが、この液体ヘリウムがタンク内で蒸発する
ので、この蒸発したヘリウムガスを冷却凝縮させて液化
する必要があり、この目的で極低温冷凍機が使用され
る。
2. Description of the Related Art Generally, in a superconductor utilizing a superconducting phenomenon, liquid helium stored in a tank is used to keep its temperature below a critical temperature. Since it evaporates in the tank, it is necessary to cool and condense the evaporated helium gas to liquefy it, and a cryogenic refrigerator is used for this purpose.

【0003】このヘリウムガスを凝縮温度まで冷却する
冷凍機の一例として、従来、例えば米国特許第4223
540号等に記載されているように、予冷冷凍機とJ−
T冷凍機とを組み合わせた冷凍機がある。上記予冷冷凍
機はGMサイクル(ギフォード・マクマホンサイクル)
や改良ソルベーサイクル等の冷凍機からなるもので、圧
縮機で圧縮されたヘリウムガス(ガス冷媒)を膨張機で
断熱膨張させてそのガスの温度降下によりヒートステー
ションに極低温レベルの寒冷を発生させる。
As an example of a refrigerator for cooling the helium gas to a condensing temperature, there is conventionally known, for example, US Pat. No. 4,223.
No. 540, etc., a pre-cooling refrigerator and a J-
There is a refrigerator combined with a T refrigerator. The above pre-cooling refrigerator is a GM cycle (Gifford McMahon cycle)
And a refrigerating machine such as an improved solve cycle. The helium gas (gas refrigerant) compressed by the compressor is adiabatically expanded by the expander, and the temperature drop of the gas causes the cryogenic cold level in the heat station. .

【0004】一方、J−T冷凍機は、圧縮機から供給さ
れたヘリウムガスを上記予冷冷凍機における膨張機のヒ
ートステーションとの間で熱交換して予冷する予冷器
と、ヘリウムガスをジュール・トムソン膨張させるJ−
T弁とを接続してなるもので、圧縮機からのヘリウムガ
スを予冷器で予冷するとともに、該予冷されたヘリウム
ガスをJ−T弁でジュール・トムソン膨張させて4Kレ
ベルの寒冷を発生させるようになっている。
On the other hand, the J-T refrigerator has a precooler for precooling by exchanging heat between the helium gas supplied from the compressor and the heat station of the expander in the precooling refrigerator, and the helium gas in a joule. Thomson inflates J-
It is connected to a T valve, and helium gas from the compressor is precooled by a precooler, and the precooled helium gas is expanded by Joule-Thomson with the JT valve to generate 4K level cold. It is like this.

【0005】[0005]

【発明が解決しようとする課題】ところで、この種の極
低温冷凍機においては、圧縮機の停止後に冷媒回路内の
圧力を均圧にして、その停止後の再起動を容易化するこ
とが行われており、その場合、圧縮機が例えばスクロー
ル圧縮機等の容積型のものであると、その均圧圧力が低
いほど圧縮機の起動トルクを小さくすることができ、そ
の作動信頼性を向上させることができる。
By the way, in this type of cryogenic refrigerator, the pressure in the refrigerant circuit is equalized after the compressor is stopped, and the restart after the stop is facilitated. In that case, if the compressor is of a positive displacement type such as a scroll compressor, the starting torque of the compressor can be made smaller as the pressure equalizing pressure is lower, and its operation reliability is improved. be able to.

【0006】しかし、冷媒回路が単純な閉じサイクルで
ある場合、その冷媒回路内で均圧に用いられる全冷媒量
は一定であるので、均圧するのに要する時間に長短の違
いはあっても、その最終的な均圧圧力自体を下げること
に限度があった。
However, when the refrigerant circuit has a simple closed cycle, the total amount of refrigerant used for equalizing the pressure in the refrigerant circuit is constant, so that there is a difference in the time required to equalize the pressure, There was a limit to lowering the final pressure equalizing pressure itself.

【0007】本発明は斯かる点に鑑みてなされたもので
あり、その目的は、一部がガス冷媒の膨張降温により液
化した液冷媒を溜める液化槽内に開放されているオープ
ンサイクルの冷媒回路に対し、その構造的な特徴を利用
することで、コストアップを招くことなく、圧縮機停止
時の冷媒回路の均圧圧力自体を低下させ、圧縮機の作動
信頼性を向上させることにある。
The present invention has been made in view of the above problems, and an object thereof is an open-cycle refrigerant circuit which is partially opened in a liquefaction tank for accumulating liquid refrigerant liquefied by expansion and cooling of the gas refrigerant. On the other hand, by utilizing the structural characteristics, the pressure equalizing pressure itself of the refrigerant circuit when the compressor is stopped is lowered without increasing the cost, and the operational reliability of the compressor is improved.

【0008】[0008]

【課題を解決するための手段】上記の目的を達成すべ
く、この発明では、圧縮機の停止時、その圧縮機と膨張
手段との間の冷媒回路を所定時間だけ開状態のまま保持
し、圧縮機側のガス冷媒を膨張手段側に流して圧縮機側
の冷媒回路におけるガス冷媒量を減少させることで、均
圧圧力そのものを低下させるようにした。
In order to achieve the above object, in the present invention, when the compressor is stopped, the refrigerant circuit between the compressor and the expansion means is kept open for a predetermined time, The pressure equalizing pressure itself is lowered by causing the gas refrigerant on the compressor side to flow toward the expansion means to reduce the amount of gas refrigerant in the refrigerant circuit on the compressor side.

【0009】具体的には、請求項1の発明では、図1〜
図3に示すように、ヘリウムガス等のガス冷媒を圧縮す
る圧縮機(4),(8)と、高圧のガス冷媒を膨張させ
て寒冷を発生させる膨張手段(41)とを高圧配管(1
5)及び低圧配管(3)により接続してなる冷媒回路
(53)と、この冷媒回路(53)の一部が内部に開放
され、液冷媒を溜める液化槽(DL )とを備え、この液
化槽(DL )内で蒸発したガス冷媒を冷媒回路(53)
に吸入して圧縮機(4),(8)で圧縮するとともに、
この圧縮されたガス冷媒を膨張手段(41)で膨張さ
せ、その膨張による温度降下により液冷媒を生成して液
化槽(DL )内に戻すようにした極低温冷凍機が前提で
ある。
Specifically, according to the invention of claim 1, FIG.
As shown in FIG. 3, compressors (4) and (8) for compressing a gas refrigerant such as helium gas and an expansion means (41) for expanding the high-pressure gas refrigerant to generate cold are provided with high-pressure piping (1).
5) and a low-pressure pipe (3) are connected to each other, and a refrigerant circuit (53) and a liquefaction tank (DL) for accumulating a liquid refrigerant in which a part of this refrigerant circuit (53) is opened are provided. Refrigerant circuit (53) for the gas refrigerant evaporated in the tank (DL)
Inhaled into and compressed with compressors (4) and (8),
It is premised on a cryogenic refrigerator in which the compressed gas refrigerant is expanded by the expansion means (41) and a temperature drop due to the expansion generates a liquid refrigerant to be returned into the liquefaction tank (DL).

【0010】そして、上記圧縮機(4),(8)と膨張
手段(41)とを連通又は連通遮断する開閉手段(5
4)と、圧縮機(4),(8)の停止から所定時間が経
過するまでの間は上記開閉手段(54)を開き、上記所
定時間の経過後に開閉手段(54)を閉じるように制御
する制御手段(61)とを設ける。
The opening / closing means (5) for connecting or disconnecting the compressors (4), (8) and the expansion means (41).
4) and the control so that the opening / closing means (54) is opened until a predetermined time elapses after the compressors (4) and (8) are stopped and the opening / closing means (54) is closed after the predetermined time elapses. And a control means (61) for controlling.

【0011】請求項2の発明では、上記制御手段(6
1)が圧縮機(4),(8)の停止後に開閉手段(5
4)を開く時間は、液化槽(DL )内部の圧力が設定圧
力に上昇するまでの時間とする。
According to a second aspect of the invention, the control means (6
After the compressors (4) and (8) are stopped, the opening and closing means (5)
4) Open the time until the pressure inside the liquefaction tank (DL) rises to the set pressure.

【0012】請求項3の発明では、図1又は図3に示す
ように、上記開閉手段(54)は、高圧配管(15)を
開閉する開閉弁(AV)と、低圧配管(3)に配設さ
れ、膨張手段(41)のガス冷媒が圧縮機(4),
(8)に戻るのは許容する一方、圧縮機(4),(8)
からガス冷媒が膨張手段(41)に移動するのは阻止す
る逆止弁(CV)とで構成されているものとする。
According to the third aspect of the invention, as shown in FIG. 1 or 3, the opening / closing means (54) is provided to the opening / closing valve (AV) for opening and closing the high pressure pipe (15) and the low pressure pipe (3). And the gas refrigerant of the expansion means (41) is installed in the compressor (4),
While permitting return to (8), compressors (4), (8)
And a check valve (CV) that prevents the gas refrigerant from moving to the expansion means (41).

【0013】請求項4の発明では、図3に示す如く、上
記開閉弁(AV)は電磁弁とする。また、請求項5の発
明では、図1に示すように、開閉弁(AV)は空気圧力
により開閉する空圧弁とする。
In the fourth aspect of the invention, as shown in FIG. 3, the on-off valve (AV) is a solenoid valve. Further, in the invention of claim 5, as shown in FIG. 1, the on-off valve (AV) is a pneumatic valve which is opened and closed by air pressure.

【0014】請求項6の発明では、極低温冷凍機の均圧
制御方法であり、上記請求項1の発明の前提の極低温冷
凍機において、圧縮機(4),(8)の停止から所定時
間が経過するまでの間は圧縮機(4),(8)と膨張手
段(41)とを連通させ、上記所定時間の経過後に圧縮
機(4),(8)と膨張手段(41)との連通を遮断す
ることを特徴としている。
According to a sixth aspect of the present invention, there is provided a method for controlling the pressure equalization of a cryogenic refrigerator. In the cryogenic refrigerator as a premise of the first aspect of the invention, the compressors (4) and (8) are stopped for a predetermined period of time. Until the time elapses, the compressors (4), (8) and the expansion means (41) are communicated with each other, and after the elapse of the predetermined time, the compressors (4), (8) and the expansion means (41) are connected. It is characterized by cutting off communication.

【0015】[0015]

【作用】上記の構成により、請求項1又は6の発明で
は、冷凍機が運転状態にあるときには、開閉手段(5
4)は開かれて圧縮機(4),(8)と膨張手段(4
1)とが連通される。この状態では、圧縮機(4),
(8)の運転に伴い、液化槽(DL )内で蒸発したガス
冷媒が冷媒回路(53)に吸入されて圧縮機(4),
(8)で圧縮され、この圧縮されたガス冷媒はその後に
膨張手段(41)で膨張によって温度降下して液冷媒と
なり、この液冷媒が液化槽(DL )内に戻される。
With the above construction, in the invention of claim 1 or 6, when the refrigerator is in the operating state, the opening / closing means (5
4) is opened and the compressors (4), (8) and the expansion means (4)
1) is communicated with. In this state, the compressor (4),
With the operation of (8), the gas refrigerant evaporated in the liquefaction tank (DL) is sucked into the refrigerant circuit (53), and the compressor (4),
The compressed gas refrigerant is compressed in (8), and the expansion means (41) thereafter expands the temperature of the gas refrigerant to lower it to a liquid refrigerant, which is returned to the liquefaction tank (DL).

【0016】この冷凍機が運転状態から停止されて圧縮
機(4),(8)が停止したとき、制御手段(61)に
より開閉手段(54)が開閉制御される。まず、その圧
縮機(4),(8)の停止から所定時間が経過するまで
の間は圧縮機(4),(8)の運転状態と同様に開閉手
段(54)が開状態に保たれる。このため、圧縮機
(4),(8)と膨張手段(41)とは連通保持され、
圧縮機(4),(8)の停止により冷媒回路(53)の
高圧配管(15)内のガス冷媒が膨張手段(41)側に
両者の差圧によって流れ、このことで冷媒回路(53)
における圧縮機(4),(8)側のガス冷媒量が減少す
る。
When the refrigerator is stopped from the operating state and the compressors (4) and (8) are stopped, the opening / closing means (54) is controlled to open / close by the control means (61). First, the opening / closing means (54) is kept open in the same manner as the operating state of the compressors (4) and (8) from the stop of the compressors (4) and (8) until a predetermined time elapses. Be done. Therefore, the compressors (4), (8) and the expansion means (41) are held in communication with each other,
By stopping the compressors (4) and (8), the gas refrigerant in the high-pressure pipe (15) of the refrigerant circuit (53) flows toward the expansion means (41) due to the pressure difference between the two, whereby the refrigerant circuit (53).
The amount of gas refrigerant on the side of the compressors (4) and (8) decreases.

【0017】次いで、圧縮機(4),(8)の停止から
所定時間が経過すると、上記開閉手段(54)が閉じら
れ、上記圧縮機(4),(8)と膨張手段(41)との
連通が開閉手段(54)によって遮断される。この遮断
により、液化槽(DL )内の圧力が圧縮機(4),
(8)側と同じ圧力で均圧することを防止でき、液化槽
(DL )の耐圧圧力を低く設定することができる。
Then, when a predetermined time has passed since the compressors (4), (8) were stopped, the opening / closing means (54) is closed, and the compressors (4), (8) and the expansion means (41) are connected. The communication of is closed by the opening / closing means (54). Due to this interruption, the pressure in the liquefaction tank (DL) is reduced to the compressor (4),
It is possible to prevent pressure equalization at the same pressure as the (8) side, and it is possible to set the withstand pressure of the liquefaction tank (DL) low.

【0018】このように、圧縮機(4),(8)の停止
時に所定時間の間だけ開閉手段(54)の閉じ動作を遅
延させて圧縮機(4),(8)と膨張手段(41)とを
連通保持し、圧縮機(4),(8)側の冷媒回路(5
3)のガス冷媒の量を減少させるので、その後に圧縮機
(4),(8)側の冷媒回路(53)でガス冷媒が均圧
になったときの均圧圧力自体を下げることができる。こ
のため、その均圧状態で圧縮機(4),(8)を再起動
するときに、その起動トルクを小さくすることができ、
圧縮機(4),(8)の作動信頼性を向上させることが
できる。
In this way, when the compressors (4) and (8) are stopped, the closing operation of the opening / closing means (54) is delayed for a predetermined time, and the compressors (4) and (8) and the expansion means (41) are delayed. ), And the refrigerant circuit (5) on the compressor (4), (8) side.
Since the amount of the gas refrigerant in 3) is reduced, the pressure equalizing pressure itself when the gas refrigerant is equalized in the refrigerant circuits (53) on the side of the compressors (4) and (8) can be reduced thereafter. . Therefore, when the compressors (4) and (8) are restarted in the pressure equalized state, the starting torque can be reduced,
The operational reliability of the compressors (4) and (8) can be improved.

【0019】また、上記開閉手段(54)は、液化槽
(DL )内の圧力の圧縮機(4),(8)側と同じ圧力
での均圧を防止するためにも使用できるので、この開閉
手段(54)の兼用化によってコストアップを招くこと
なく、上記効果が得られる。
The opening / closing means (54) can also be used to prevent equalization of the pressure in the liquefaction tank (DL) at the same pressure as that on the compressor (4), (8) side. The above effect can be obtained without increasing the cost due to the dual use of the opening / closing means (54).

【0020】請求項2の発明では、圧縮機(4),
(8)の停止から開閉手段(54)が開かれるまでの時
間は、液化槽(DL )内部の圧力が設定圧力に上昇する
までの時間であるので、液化槽(DL )内部の圧力が設
定圧力に上昇すると、開閉手段(54)が閉じられるこ
とになり、液化槽(DL )内部の圧力が設定圧力を越え
て上昇するのを確実に防止することができる。
In the invention of claim 2, the compressor (4),
Since the time from the stop of (8) until the opening / closing means (54) is opened is the time until the pressure inside the liquefaction tank (DL) rises to the set pressure, the pressure inside the liquefaction tank (DL) is set. When the pressure rises, the opening / closing means (54) is closed, and it is possible to reliably prevent the pressure inside the liquefaction tank (DL) from rising above the set pressure.

【0021】請求項3の発明では、開閉手段(54)
は、高圧配管(15)を開閉する開閉弁(AV)と、低
圧配管(3)に配設された逆止弁(CV)とで構成され
ているので、そのうちの開閉弁(AV)のみを開閉動作
させるだけで圧縮機(4),(8)と膨張手段(41)
との連通又は連通遮断を切り換えることができ、開閉手
段(54)の構成を簡略にすることができる。
In the invention of claim 3, the opening / closing means (54)
Is composed of an on-off valve (AV) that opens and closes the high-pressure pipe (15) and a check valve (CV) arranged on the low-pressure pipe (3). Compressors (4), (8) and expansion means (41) are simply opened and closed.
It is possible to switch between communication with and disconnection of communication, and the structure of the opening / closing means (54) can be simplified.

【0022】請求項4の発明では、開閉弁(AV)は電
磁弁であり、請求項5の発明では、開閉弁(AV)は空
圧弁であるので、開閉弁(AV)の具体的構成が得られ
る。特に、請求項5の発明のように、空気圧力により開
閉する空圧弁を用いると、磁場等の影響があっても開閉
弁(AV)を誤動作することなく安定して開閉させるこ
とができる。
In the invention of claim 4, the opening / closing valve (AV) is an electromagnetic valve, and in the invention of claim 5, the opening / closing valve (AV) is a pneumatic valve. Therefore, the specific structure of the opening / closing valve (AV) is can get. In particular, when the pneumatic valve that opens and closes by the air pressure is used as in the fifth aspect of the present invention, the on-off valve (AV) can be stably opened and closed without malfunctioning even when affected by a magnetic field or the like.

【0023】[0023]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。 (実施例1)図2は本発明の実施例1に係る冷凍機
(R)の全体構成を示し、この冷凍機(R)は圧縮機ユ
ニット(1)と、真空槽(D)内に配置される冷凍機ユ
ニット(31)とからなる。
Embodiments of the present invention will be described below with reference to the drawings. (Embodiment 1) FIG. 2 shows the entire structure of a refrigerator (R) according to Embodiment 1 of the present invention. This refrigerator (R) is arranged in a compressor unit (1) and a vacuum chamber (D). And a refrigerator unit (31).

【0024】上記圧縮機ユニット(1)には、低圧ガス
吸入口(2)からの低圧ヘリウムガスを低圧配管(3)
を介して吸い込んで圧縮する低段用圧縮機(4)と、こ
の低段用圧縮機(4)から吐出されたヘリウムガスを冷
却する熱交換器(5)と、この熱交換器(5)から吐出
されたヘリウムガスを、中間圧ガス吸入口(6)から中
間圧配管(7)を介して吸入された中間圧のヘリウムガ
スと共にさらに高圧に圧縮する高段用圧縮機(8)と、
この高段用圧縮機(8)から吐出された高圧ヘリウムガ
スから圧縮機潤滑用の油を分離する前段油分離器(9)
と、この前段油分離器(9)から吐出された高圧ヘリウ
ムガスを冷却する熱交換器(10)と、この熱交換器
(10)から吐出されたヘリウムガスからさらに潤滑用
の油を分離する後段油分離器(11)と、この後段油分
離器(11)から吐出されたヘリウムガスから不純物を
吸着除去する吸着器(12)とが配設され、該吸着器
(12)の吐出側に高圧配管(13)の一端が接続され
ている。この高圧配管(13)の他端側は予冷用高圧配
管(14)及びJ−T用高圧配管(15)に分岐され、
予冷用高圧配管(14)は予冷用高圧ガス吐出口(1
6)に、またJ−T用高圧配管(15)はJ−T用高圧
ガス吐出口(17)にそれぞれ接続されている。
In the compressor unit (1), low pressure helium gas from the low pressure gas inlet (2) is supplied to the low pressure pipe (3).
Low-stage compressor (4) that sucks in through the compressor and compresses it, a heat exchanger (5) that cools helium gas discharged from the low-stage compressor (4), and this heat exchanger (5) A high-stage compressor (8) for further compressing the helium gas discharged from the intermediate pressure gas suction port (6) to a higher pressure together with the intermediate pressure helium gas sucked through the intermediate pressure pipe (7);
A pre-stage oil separator (9) for separating oil for compressor lubrication from the high-pressure helium gas discharged from the high-stage compressor (8).
And a heat exchanger (10) for cooling the high-pressure helium gas discharged from the former oil separator (9), and further separating lubricating oil from the helium gas discharged from the heat exchanger (10). A post-stage oil separator (11) and an adsorber (12) for adsorbing and removing impurities from the helium gas discharged from the post-stage oil separator (11) are provided, and the adsorbing side of the adsorber (12) is provided. One end of the high pressure pipe (13) is connected. The other end of the high-pressure pipe (13) is branched into a pre-cooling high-pressure pipe (14) and a JT high-pressure pipe (15),
The high-pressure pipe for pre-cooling (14) is a high-pressure gas outlet for pre-cooling (1
6) and the JT high-pressure pipe (15) is connected to the JT high-pressure gas discharge port (17).

【0025】さらに、上記低段用圧縮機(4)の吸込側
と低圧ガス吸入口(2)との間の低圧配管(3)にはヘ
リウムガス供給配管(18)の一端が分岐接続されてい
る。また、上記高圧配管(13)の一部であるJ−T用
高圧配管(15)には高圧制御弁(HPR)を配置した
ヘリウムガス戻し配管(20)の一端が分岐接続され、
このヘリウムガス戻し配管(20)の他端は上記ヘリウ
ムガス供給配管(18)の他端と集合されてヘリウムガ
ス給排配管(21)の一端に接続され、このヘリウムガ
ス給排配管(21)の他端は、ヘリウムガスを所定圧力
で貯蔵するバッファタンク(Tb)に接続されている。
Further, one end of a helium gas supply pipe (18) is branched and connected to the low-pressure pipe (3) between the suction side of the low-stage compressor (4) and the low-pressure gas suction port (2). There is. Further, one end of a helium gas return pipe (20) in which a high pressure control valve (HPR) is arranged is branched and connected to the JT high pressure pipe (15) which is a part of the high pressure pipe (13).
The other end of the helium gas return pipe (20) is assembled with the other end of the helium gas supply pipe (18) and connected to one end of the helium gas supply / discharge pipe (21). The other end of is connected to a buffer tank (Tb) that stores helium gas at a predetermined pressure.

【0026】上記高圧制御弁(HPR)は、高圧配管
(13)(J−T用高圧配管(15))でのヘリウムガ
スの圧力が設定圧以上に上昇したときにそれをパイロッ
ト圧として自動的に開くもので、この高圧制御弁(HP
R)の開弁によりJ−T用高圧配管(15)(後述の冷
媒回路(53))のヘリウムガスがバッファタンク(T
b)内に回収される。
The high-pressure control valve (HPR) automatically uses the helium gas in the high-pressure pipe (13) (JT high-pressure pipe (15)) as a pilot pressure when it rises above a set pressure. This high pressure control valve (HP
By opening the valve (R), the helium gas in the JT high-pressure pipe (15) (refrigerant circuit (53) described later) is transferred to the buffer tank (T).
Recovered in b).

【0027】上記ヘリウムガス供給配管(18)は途中
で2つの分岐配管(18a),(18b)に並列に分岐
され、一方の分岐配管(18a)には流路閉止用の絞り
固定式の閉止弁(V2)と、この閉止弁(V2)の低圧
配管(3)側に常時閉の第1低圧制御弁(LPR1)と
が配設されている一方、他方の分岐配管(18b)には
同様の閉止弁(V3)と常時閉の第2低圧制御弁(LP
R2)とが配設されている。上記各低圧制御弁(LPR
1),(LPR2)は、低圧配管(3)でのヘリウムガ
スの圧力が設定圧以下に低下したときにそれをパイロッ
ト圧として自動的に開くもので、この低圧制御弁(LP
R1),(LPR2)の開弁に伴いバッファタンク(T
b)内のヘリウムガスが低圧配管(3)(冷媒回路(5
3))に供給される。
The helium gas supply pipe (18) is branched into two branch pipes (18a) and (18b) in parallel on the way, and one of the branch pipes (18a) is fixed by a throttle for closing the flow passage. The valve (V2) and the normally closed first low pressure control valve (LPR1) are arranged on the low pressure pipe (3) side of the shutoff valve (V2), while the other branch pipe (18b) is the same. Shut-off valve (V3) and normally closed second low-pressure control valve (LP
R2) are provided. Each low pressure control valve (LPR
1) and (LPR2) automatically open as a pilot pressure when the pressure of helium gas in the low pressure pipe (3) drops below a set pressure.
The buffer tank (T
The helium gas in b) is the low pressure pipe (3) (refrigerant circuit (5
3)).

【0028】これに対し、上記冷凍機ユニット(31)
には、圧縮機ユニット(1)の高段用圧縮機(8)に対
し閉回路に接続された予冷冷凍機(32)と、低段用圧
縮機(4)及び高段用圧縮機(8)に対し直列に接続さ
れたJ−T冷凍機(41)(膨張手段)とが設置されて
いる。上記予冷冷凍機(32)は、G−M(ギフォード
・マクマホン)サイクルの冷凍機で構成されていて、J
−T冷凍機(41)におけるヘリウムガス(ガス冷媒)
を予冷するためにヘリウムガスを圧縮及び膨張させる。
この予冷冷凍機(32)は上記真空槽(D)の外部に配
置される密閉円筒状のケース(33)と、該ケース(3
3)に連設された大小2段構造のシリンダ(34)とを
有する。上記ケース(33)には上記圧縮機ユニット
(1)の予冷用高圧ガス吐出口(16)にフレキシブル
配管(35)を介して接続される高圧ガス入口(36)
と、同中間圧ガス吸入口(6)にフレキシブル配管(3
7)を介して接続される低圧ガス出口(38)とが開口
されている。一方、シリンダ(34)は真空槽(D)の
側壁を貫通してその内部に延びており、その大径部(3
4a)の先端部は所定温度レベルに冷却保持される第1
ヒートステーション(39)に、また小径部(34b)
の先端部は上記第1ヒートステーション(39)よりも
低い温度レベルに冷却保持される第2ヒートステーショ
ン(40)にそれぞれ形成されている。
On the other hand, the refrigerator unit (31)
Includes a precooling refrigerator (32) connected to the high-stage compressor (8) of the compressor unit (1) in a closed circuit, a low-stage compressor (4) and a high-stage compressor (8). ) Is connected in series with the JT refrigerator (41) (expansion means). The pre-cooling refrigerator (32) is composed of a G-M (Gifford McMahon) cycle refrigerator.
Helium gas (gas refrigerant) in the -T refrigerator (41)
The helium gas is compressed and expanded to precool it.
The pre-cooling refrigerator (32) has a closed cylindrical case (33) arranged outside the vacuum chamber (D), and the case (3).
3) and a cylinder (34) having a large and small two-stage structure that is continuously provided. In the case (33), a high pressure gas inlet (36) connected to the precooling high pressure gas discharge port (16) of the compressor unit (1) through a flexible pipe (35).
And the flexible pipe (3) at the intermediate pressure gas inlet (6).
The low pressure gas outlet (38) connected via 7) is open. On the other hand, the cylinder (34) penetrates the side wall of the vacuum chamber (D) and extends inside thereof, and has a large diameter portion (3
The tip of 4a) is cooled and maintained at a predetermined temperature level.
Heat station (39) and small diameter part (34b)
Of the first heat station (39) is formed in the second heat station (40) cooled and maintained at a temperature level lower than that of the first heat station (39).

【0029】すなわち、ここでは図示しないが、シリン
ダ(34)内には、上記各ヒートステーション(3
9),(40)に対応する位置にそれぞれ膨張空間を区
画形成するフリータイプのディスプレーサ(置換器)が
往復動可能に嵌挿されている。一方、上記ケース(3
3)内には、回転する毎に開閉するロータリバルブと、
該ロータリバルブを駆動するバルブモータとが収容され
ている。ロータリバルブは、上記高圧ガス入口(36)
から流入したヘリウムガスをシリンダ(34)内の各膨
張空間に供給し、又は各膨張空間内で膨張したヘリウム
ガスを低圧ガス出口(38)から排出するように切り換
わる。そして、このロータリバルブの開閉により高圧ヘ
リウムガスをシリンダ(34)内の各膨張空間でサイモ
ン膨張させて、その膨張に伴う温度降下により極低温レ
ベルの寒冷を発生させ、その寒冷をシリンダ(34)に
おける第1及び第2ヒートステーション(39),(4
0)にて保持する。つまり、予冷冷凍機(32)では、
高段用圧縮機(8)から吐出された高圧のヘリウムガス
を断熱膨張させてヒートステーション(39),(4
0)の温度を低下させ、J−T冷凍機(41)における
後述の予冷器(46),(47)を予冷するとともに、
膨張した低圧ヘリウムガスを圧縮機(8)に戻して再圧
縮するようになされている。
That is, although not shown here, in the cylinder (34), each heat station (3
Free-type displacers (replacers) that partition and form the expansion spaces are reciprocally fitted at positions corresponding to 9) and (40). On the other hand, the above case (3
In 3), a rotary valve that opens and closes each time it rotates,
A valve motor that drives the rotary valve is housed. The rotary valve has the high pressure gas inlet (36).
The helium gas flowing in from is supplied to each expansion space in the cylinder (34), or the helium gas expanded in each expansion space is switched to be discharged from the low pressure gas outlet (38). Then, by opening and closing this rotary valve, the high-pressure helium gas is expanded by Simon in each expansion space in the cylinder (34), and a temperature drop due to the expansion causes a cryogenic level of cold to be generated, and the cold is cooled by the cylinder (34). First and second heat stations (39), (4
Hold at 0). That is, in the pre-cooling refrigerator (32),
The high-pressure helium gas discharged from the high-stage compressor (8) is adiabatically expanded to heat stations (39), (4
0) to lower the temperature to precool later-described precoolers (46) and (47) in the J-T refrigerator (41),
The expanded low pressure helium gas is returned to the compressor (8) and recompressed.

【0030】一方、上記J−T冷凍機(41)は、約4
Kレベルの寒冷を発生させるためにヘリウムガスをジュ
ール・トムソン膨張させる冷凍機であって、この冷凍機
(41)は上記真空槽(D)内に配置された第1〜第3
のJ−T熱交換器(42)〜(44)を備えている。こ
の各J−T熱交換器(42)〜(44)は1次側及び2
次側をそれぞれ通過するヘリウムガス間で互いに熱交換
させるもので、第1J−T熱交換器(42)の1次側は
圧縮機ユニット(1)のJ−T用高圧ガス吐出口(1
7)にフレキシブル配管(45)を介して接続されてい
る。また、第1及び第2のJ−T熱交換器(42),
(43)の各1次側同士は、上記予冷冷凍機(32)に
おけるシリンダ(34)の第1ヒートステーション(3
9)外周に配置した第1予冷器(46)を介して接続さ
れている。同様に、第2及び第3J−T熱交換器(4
3),(44)の各1次側同士は、第2ヒートステーシ
ョン(40)外周に配置した第2予冷器(47)を介し
て接続されている。さらに、上記第3J−T熱交換器
(44)の1次側は、高圧のヘリウムガスをジュール・
トムソン膨張させるJ−T弁(48)に吸着器(49)
を介して接続されている。このJ−T弁(48)は、液
体ヘリウム戻し配管(50)を介して液化槽(DL )内
に連通されている。この液化槽(DL )は所定量の液体
ヘリウムを貯溜するもので、この液体ヘリウムにより図
外の冷却対象物を極低温レベルに冷却する。また、液化
槽(DL )の内部は、ヘリウムガス吸入配管(51)を
介して上記第3J−T熱交換器(44)の2次側に接続
されている。そして、この第3J−T熱交換器(44)
の2次側は第2J−T熱交換器(43)の2次側を経て
第1J−T熱交換器(42)の2次側に接続され、この
第1J−T熱交換器(42)の2次側はフレキシブル配
管(52)を介して圧縮機ユニット(1)の低圧ガス吸
入口(2)に接続されている。
On the other hand, the JT refrigerator (41) has about 4
A refrigerator that expands helium gas by Joule-Thomson in order to generate K-level cold, and the refrigerator (41) is a first to third refrigerator arranged in the vacuum chamber (D).
JT heat exchangers (42) to (44). Each of the JT heat exchangers (42) to (44) has a primary side and a secondary side.
The helium gas passing through each of the secondary sides exchanges heat with each other. The primary side of the first JT heat exchanger (42) has a high pressure gas discharge port (1) for JT of the compressor unit (1).
7) via a flexible pipe (45). Also, the first and second JT heat exchangers (42),
The respective primary sides of (43) are connected to the first heat station (3) of the cylinder (34) in the precooling refrigerator (32).
9) It is connected via a first precooler (46) arranged on the outer circumference. Similarly, the second and third J-T heat exchangers (4
The respective primary sides of 3) and (44) are connected to each other via a second precooler (47) arranged on the outer periphery of the second heat station (40). Further, the primary side of the third J-T heat exchanger (44) uses high-pressure helium gas as a joule.
Adsorber (49) to JT valve (48) to expand Thomson
Connected through. The JT valve (48) is connected to the liquefaction tank (DL) via a liquid helium return pipe (50). The liquefaction tank (DL) stores a predetermined amount of liquid helium, and the liquid helium cools an object to be cooled (not shown) to a cryogenic level. Further, the inside of the liquefaction tank (DL) is connected to the secondary side of the third JT heat exchanger (44) through a helium gas suction pipe (51). And this 3rd J-T heat exchanger (44)
Is connected to the secondary side of the first J-T heat exchanger (42) through the secondary side of the second J-T heat exchanger (43), and the first J-T heat exchanger (42) is connected. The secondary side of is connected to the low-pressure gas suction port (2) of the compressor unit (1) via a flexible pipe (52).

【0031】すなわち、J−T冷凍機(41)はフレキ
シブル配管(45),(52)、低圧配管(3)、両圧
縮機(4),(8)及び高圧配管(3)のJ−T用高圧
配管(15)に対し直列に接続された冷媒回路(53)
をなし、この冷媒回路(53)は一部が液化槽(DL )
内に開放されたオープンサイクルとされており、冷却対
象物の熱負荷により液化槽(DL )内で蒸発したヘリウ
ムガスをヘリウムガス吸入配管(51)から冷媒回路
(53)に吸い込んで第3〜第1J−T熱交換器(4
4)〜(42)の各2次側を通して低段用及び高段用圧
縮機(4),(8)に吸入圧縮する一方、その高段用圧
縮機(8)により圧縮された高圧ヘリウムガスを第1〜
第3のJ−T熱交換器(42)〜(44)において、圧
縮機(4)側に向かう低温低圧のヘリウムガスと熱交換
させ、かつ第1及び第2予冷器(46),(47)でそ
れぞれシリンダ(34)の第1及び第2ヒートステーシ
ョン(39),(40)で冷却した後、J−T弁(4
8)でジュール・トムソン膨張させて約4Kの液状態の
ヘリウムとなし、この液体ヘリウムを液体ヘリウム戻し
配管(50)を経て液化槽(DL )に戻すようになされ
ている。尚、上記J−T弁(48)は真空槽(D)外側
から操作ロッド(48a)によって開度が調整される。
That is, the JT refrigerator (41) is a flexible pipe (45), (52), low pressure pipe (3), both compressors (4), (8) and high pressure pipe (3) JT. Refrigerant circuit (53) connected in series to the high pressure pipe (15) for use
This refrigerant circuit (53) is partly a liquefaction tank (DL)
The helium gas evaporated in the liquefaction tank (DL) due to the heat load of the object to be cooled is sucked into the refrigerant circuit (53) from the helium gas suction pipe (51) and the third to 1st J-T heat exchanger (4
High-pressure helium gas compressed by the high-stage compressor (8) while being sucked and compressed into the low-stage and high-stage compressors (4) and (8) through the secondary sides of 4) to (42). The first
In the third JT heat exchangers (42) to (44), heat is exchanged with the low-temperature low-pressure helium gas toward the compressor (4) side, and the first and second precoolers (46), (47). ), Respectively, at the first and second heat stations (39) and (40) of the cylinder (34), and then the JT valve (4)
In 8), Joule-Thomson expansion is performed to form liquid helium of about 4K, and this liquid helium is returned to the liquefaction tank (DL) through the liquid helium return pipe (50). The opening of the JT valve (48) is adjusted by the operation rod (48a) from the outside of the vacuum chamber (D).

【0032】図1に拡大詳示するように、上記J−T用
高圧配管(15)の途中には流量調整用の絞り固定式の
絞り弁(V1)と、この絞り弁(V1)の吸着器(1
2)側に高圧配管(15)を開閉する開閉弁(AV)と
が配設され、この開閉弁(AV)は空気圧力により開閉
する空圧弁からなる。
As shown in an enlarged detail in FIG. 1, a fixed throttle type throttle valve (V1) for adjusting the flow rate and an adsorption of this throttle valve (V1) are provided in the middle of the JT high-pressure pipe (15). Bowl (1
An on-off valve (AV) that opens and closes the high-pressure pipe (15) is provided on the 2) side, and this on-off valve (AV) is a pneumatic valve that opens and closes by air pressure.

【0033】また、ヘリウムガス供給配管(18)との
接続部よりも低圧ガス吸込口(2)側(上流側)の低圧
配管(3)の途中には逆止弁(CV)が配設され、この
逆止弁(CV)は、J−T冷凍機(41)側のヘリウム
ガスが圧縮機(4),(8)に戻るのは許容する一方、
圧縮機(4),(8)からヘリウムガスがJ−T冷凍機
(41)に移動するのは阻止する機能を有する。そし
て、この実施例では、上記開閉弁(AV)及び逆止弁
(CV)により、圧縮機(4),(8)とJ−T冷凍機
(41)とを連通又は連通遮断する開閉機構(54)が
構成されている。
A check valve (CV) is provided in the middle of the low-pressure pipe (3) on the low-pressure gas inlet (2) side (upstream side) of the connection with the helium gas supply pipe (18). While the check valve (CV) allows the helium gas on the JT refrigerator (41) side to return to the compressors (4) and (8),
It has a function of preventing helium gas from moving from the compressors (4) and (8) to the JT refrigerator (41). In this embodiment, the opening / closing mechanism (V) and the check valve (CV) for connecting or disconnecting the compressors (4), (8) and the JT refrigerator (41) are used. 54) is configured.

【0034】上記開閉弁(AV)には空気配管(55)
を介して空圧源(56)が接続され、上記空気配管(5
5)の途中には、制御装置(61)からの電気制御信号
を受けて空圧源(56)からの空気圧力の開閉弁(A
V)への作用又は作用停止を切り換えて開閉弁(AV)
を開閉するための空圧用電磁弁(57)が配設されてい
る。また、上記制御装置(61)には、信号線を図示し
ないが、上記高段用圧縮機(8)から吐出された高圧ヘ
リウムガスの圧力を検出する高圧スイッチ(HPS)の
検出信号と、低段用圧縮機(4)の吸込側に連通する低
圧配管(3)内の低圧ヘリウムガスの圧力を検出する低
圧スイッチ(LPS)の検出信号と、ヘリウムガス給排
配管(21)内の圧力(バッファタンク(Tb)の内
圧)を検出する中圧スイッチ(MPS)の検出信号と、
圧縮機ユニット(1)における3つの保護スイッチ(S
S1)〜(SS3)の作動信号とが入力されている。
The on-off valve (AV) has an air pipe (55).
The air pressure source (56) is connected via the
In the middle of 5), an on-off valve (A) for receiving air pressure from the air pressure source (56) in response to an electric control signal from the control device (61).
Open / close valve (AV) by switching the action or stop of action on V)
A pneumatic solenoid valve (57) for opening and closing is provided. Although not shown in the figure, a signal line is not shown in the control device (61), and a detection signal of a high pressure switch (HPS) for detecting the pressure of the high pressure helium gas discharged from the high pressure compressor (8) and a low signal. The detection signal of the low pressure switch (LPS) for detecting the pressure of the low pressure helium gas in the low pressure pipe (3) communicating with the suction side of the stage compressor (4), and the pressure in the helium gas supply / discharge pipe (21) ( A detection signal of a medium pressure switch (MPS) for detecting the internal pressure of the buffer tank (Tb),
Three protection switches (S
The operation signals of S1) to (SS3) are input.

【0035】すなわち、上記制御装置(61)は制御手
段を構成するもので、この制御装置(61)において開
閉弁(AV)を空圧用電磁弁(57)を介して開閉制御
し、圧縮機(4),(8)の運転中は開閉弁(AV)を
開いて圧縮機(4),(8)とJ−T冷凍機(41)と
を連通させる一方、この圧縮機(4),(8)を運転状
態から停止させるときには、その圧縮機(4),(8)
の停止から所定時間が経過するまでの間、詳しくは圧縮
機(4),(8)の停止に伴う冷媒回路(53)での均
圧によって液化槽(DL )内部の圧力が設定圧力に上昇
するまでの時間、圧縮機(4),(8)の運転状態と同
様に開閉弁(AV)を開状態に保持し、上記所定時間が
経過した後に開閉弁(AV)を閉じるようになされてい
る。
That is, the control device (61) constitutes a control means, and in this control device (61), the opening / closing valve (AV) is controlled to open / close via the pneumatic solenoid valve (57), and the compressor ( During operation of 4) and 8), the on-off valve (AV) is opened to connect the compressors (4) and (8) to the JT refrigerator (41), while the compressors (4) and (8) are communicated. 8) is stopped from the operating state, the compressor (4), (8)
From the stop of the compressor until the predetermined time elapses, in detail, the pressure inside the liquefaction tank (DL) rises to the set pressure due to the pressure equalization in the refrigerant circuit (53) accompanying the stop of the compressors (4) and (8). The opening / closing valve (AV) is held in the open state in the same manner as the operating states of the compressors (4) and (8) until the time is reached, and the opening / closing valve (AV) is closed after the lapse of the predetermined time. There is.

【0036】尚、図2中、(24)は前段油分離器
(9)でヘリウムガスから分離された油の一部と後段油
分離器(11)で分離された油とを、低段用圧縮機
(4)から吐出されて高段用圧縮機(8)に吸入される
ヘリウムガス中にインジェクションする油戻し配管、
(25)は前段油分離器(9)で分離された油の残部を
高段用圧縮機(8)に戻す油戻し配管、(26)は高段
用圧縮機(8)内下部の油を上記油戻し配管(25)に
供給して同圧縮機(8)内上部にインジェクションする
ための油インジェクション配管、(27)は低段用圧縮
機(4)内下部の油を同圧縮機(4)内上部にインジェ
クションする油インジェクション配管、(28)は両圧
縮機(4),(8)内下部間を連通して両者の油面レベ
ルを一定にするための均油管である。
In FIG. 2, reference numeral (24) denotes a part of the oil separated from the helium gas in the former oil separator (9) and the oil separated in the latter oil separator (11) for the lower stage. An oil return pipe for injecting into helium gas discharged from the compressor (4) and sucked into the high-stage compressor (8),
(25) is an oil return pipe for returning the remaining part of the oil separated by the former-stage oil separator (9) to the high-stage compressor (8), and (26) is an oil lower part inside the high-stage compressor (8). An oil injection pipe for supplying the oil to the oil return pipe (25) to inject the oil into the upper part of the compressor (8), and (27) shows oil in the lower part of the low stage compressor (4). ) An oil injection pipe for injecting into the upper part of the inside, and (28) is an oil equalizing pipe for communicating between the lower parts of both compressors (4) and (8) to keep the oil level of both compressors constant.

【0037】次に、上記実施例の作用について説明す
る。冷凍機(R)が運転状態にあると、圧縮機ユニット
(1)の高段用圧縮機(8)から供給された高圧のヘリ
ウムガスの一部が予冷冷凍機(32)に供給される。こ
のヘリウムガスは該予冷冷凍機(32)におけるシリン
ダ(34)内の各膨張空間で膨張し、このガスの膨張に
伴う温度降下により第1ヒートステーション(39)が
所定温度レベルに、また第2ヒートステーション(4
0)が第1ヒートステーション(39)よりも低い温度
レベルにそれぞれ冷却される。膨張空間で膨張したヘリ
ウムガスは圧縮機ユニット(1)に戻り、その中間圧配
管(7)を経由して高段用圧縮機(8)に吸い込まれて
圧縮される。
Next, the operation of the above embodiment will be described. When the refrigerator (R) is in an operating state, a part of the high-pressure helium gas supplied from the high-stage compressor (8) of the compressor unit (1) is supplied to the pre-cooling refrigerator (32). The helium gas expands in each expansion space in the cylinder (34) of the precooling refrigerator (32), and the temperature drop caused by the expansion of the gas causes the first heat station (39) to reach a predetermined temperature level and the second heat station (39). Heat station (4
0) are each cooled to a lower temperature level than the first heat station (39). The helium gas expanded in the expansion space returns to the compressor unit (1), is sucked into the high-stage compressor (8) through the intermediate pressure pipe (7), and is compressed.

【0038】一方、圧縮機ユニット(1)におけるJ−
T用高圧配管(15)の開閉弁(AV)が制御装置(6
1)によって開かれて高段用圧縮機(8)がJ−T冷凍
機(41)に連通され、上記高段用圧縮機(8)から吐
出された高圧のヘリウムガスの残部がJ−T用高圧配管
(15)の絞り弁(V1)を経由してJ−T冷凍機(4
1)の第1J−T熱交換器(42)の1次側に入り、そ
こで圧縮機(4)側へ向かう2次側の低圧ヘリウムガス
と熱交換されて常温300Kから例えば約50Kまで冷
却され、その後、上記予冷冷凍機(32)の第1ヒート
ステーション(39)外周の第1予冷器(46)に入っ
てさらに冷却される。この冷却されたガスは第2J−T
熱交換器(43)の1次側に入って、同様に2次側の低
圧ヘリウムガスとの熱交換により例えば約15Kまで冷
却された後、予冷冷凍機(32)の第2ヒートステーシ
ョン(40)外周の第2予冷器(47)に入ってさらに
冷却される。この後、ガスは第3J−T熱交換器(4
4)の1次側に入って2次側の低圧ヘリウムガスとの熱
交換によりさらに冷却され、しかる後にJ−T弁(4
8)に至る。このJ−T弁(48)では高圧ヘリウムガ
スは絞られてジュール・トムソン膨張し、約4Kの液状
態のヘリウムとなり、この液体ヘリウムは液体ヘリウム
戻し配管(50)を介して液化槽(DL )に供給され
る。一方、液化槽(DL )内の液体ヘリウムの一部は冷
却対象物の熱負荷によって蒸発し、この液化槽(DL )
内の蒸発ヘリウムガスはヘリウムガス吸入配管(51)
を介して第3J−T熱交換器(44)の2次側に吸入さ
れ、第2及び第1J−T熱交換器(43),(42)の
各2次側を経由して低段用圧縮機(4)に吸い込まれて
圧縮される。
On the other hand, J- in the compressor unit (1)
The on-off valve (AV) of the T high-pressure pipe (15) is connected to the control device (6
1) the high-stage compressor (8) is opened to communicate with the JT refrigerator (41), and the remaining high-pressure helium gas discharged from the high-stage compressor (8) is JT. Via the throttle valve (V1) of the high pressure piping (15) for the JT refrigerator (4
1) Enter the primary side of the first J-T heat exchanger (42), where it is heat-exchanged with the low-pressure helium gas on the secondary side toward the compressor (4) side and cooled from room temperature 300K to, for example, about 50K. After that, the first precooler (46) around the outer periphery of the first heat station (39) of the precooling refrigerator (32) is further cooled. This cooled gas is the second JT
After entering the primary side of the heat exchanger (43) and being cooled to, for example, about 15K by heat exchange with the low-pressure helium gas on the secondary side as well, the second heat station (40) of the precooling refrigerator (32). ) It enters the second precooler (47) on the outer periphery and is further cooled. After this, the gas is transferred to the third JT heat exchanger (4
4) enters the primary side and is further cooled by heat exchange with the low pressure helium gas on the secondary side, and then the JT valve (4
8). In this JT valve (48), the high-pressure helium gas is squeezed and expanded by Joule-Thomson into liquid helium of about 4K, and this liquid helium is liquefied (DL) via the liquid helium return pipe (50). Is supplied to. On the other hand, part of the liquid helium in the liquefaction tank (DL) evaporates due to the heat load of the object to be cooled, and this liquefaction tank (DL)
The evaporated helium gas in the helium gas suction pipe (51)
Is sucked into the secondary side of the third J-T heat exchanger (44) through the secondary side of each of the second and first J-T heat exchangers (43) and (42). It is sucked into the compressor (4) and compressed.

【0039】斯かる冷凍機(R)の運転中、圧縮機
(4),(8)が停止されて冷凍機(R)の運転が停止
したとき、その圧縮機(4),(8)の停止から所定時
間が経過するまでの間、それまでの圧縮機(4),
(8)の運転状態と同様に開閉弁(AV)が開かれ、J
−T用高圧配管(15)が開状態に保たれて高段用圧縮
機(8)とJ−T冷凍機(41)とは連通保持される。
そして、圧縮機(4),(8)の停止直後は冷媒回路
(53)のJ−T用高圧配管(15)内の圧力はJ−T
冷凍機(41)側の圧力よりも高いので、両者の差圧に
よってJ−T用高圧配管(15)内のヘリウムガスがJ
−T冷凍機(41)側に流れ、このことで圧縮機
(4),(8)側のヘリウムガス量が減少する。尚、低
圧配管(3)には逆止弁(CV)が配設されているの
で、圧縮機(4)の吸込側がJ−T冷凍機(41)側よ
りも高圧になったとしても、圧縮機(4)側のヘリウム
ガスがJ−T冷凍機(41)側に戻ることはない。
During operation of the refrigerator (R), when the compressors (4), (8) are stopped and the operation of the refrigerator (R) is stopped, the compressors (4), (8) During the period from the stop until a predetermined time elapses, the compressor (4) until then,
The open / close valve (AV) is opened in the same manner as in the operating state of (8), and J
The -T high-pressure pipe (15) is kept open, and the high-stage compressor (8) and the JT refrigerator (41) are held in communication with each other.
Immediately after the compressors (4) and (8) are stopped, the pressure in the JT high-pressure pipe (15) of the refrigerant circuit (53) is JT.
Since the pressure is higher than the pressure on the refrigerator (41) side, the helium gas in the JT high-pressure pipe (15) is J due to the pressure difference between the two.
It flows to the −T refrigerator (41) side, which reduces the amount of helium gas on the compressor (4), (8) side. Since the check valve (CV) is arranged in the low pressure pipe (3), even if the suction side of the compressor (4) becomes higher in pressure than the JT refrigerator (41) side, the compression is performed. Helium gas on the machine (4) side never returns to the JT refrigerator (41) side.

【0040】そして、上記圧縮機(4),(8)の停止
から所定時間が経過すると開閉弁(AV)が閉じられ、
上記圧縮機(4),(8)とJ−T冷凍機(41)との
連通が開閉弁(AV)によって遮断される。この遮断に
より、液化槽(DL )内の圧力が圧縮機(4),(8)
側と同じ圧力で均圧することを防止することができる。
When a predetermined time has passed since the compressors (4) and (8) were stopped, the on-off valve (AV) is closed,
The on-off valve (AV) blocks communication between the compressors (4) and (8) and the JT refrigerator (41). Due to this interruption, the pressure in the liquefaction tank (DL) is reduced to the compressors (4), (8).
It is possible to prevent pressure equalization with the same pressure as the side.

【0041】その際、圧縮機(4),(8)の停止から
開閉弁(AV)が開弁保持される時間は、液化槽(DL
)内部の圧力が設定圧力に上昇するまでの時間である
ので、液化槽(DL )内部の圧力が設定圧力に上昇する
と、開閉弁(AV)が閉じられることとなる。よって、
液化槽(DL )内部の圧力が設定圧力を越えて上昇する
のを確実に防止することができる。
At this time, the time during which the open / close valve (AV) is held open after the compressors (4) and (8) are stopped is the liquefaction tank (DL).
Since it is the time until the internal pressure rises to the set pressure, when the internal pressure of the liquefaction tank (DL) rises to the set pressure, the on-off valve (AV) will be closed. Therefore,
It is possible to reliably prevent the pressure inside the liquefaction tank (DL) from rising above the set pressure.

【0042】この実施例では、圧縮機(4),(8)の
停止時に所定時間の間だけ開閉弁(AV)を開いて圧縮
機(4),(8)とJ−T冷凍機(41)とを連通保持
し、圧縮機(4),(8)側のヘリウムガスを減少させ
るので、その後、開閉弁(AV)が閉弁された状態で圧
縮機(4),(8)側の冷媒回路(53)のヘリウムガ
スが均圧になったときの均圧圧力を下げることができ
る。このため、その均圧状態で圧縮機(4),(8)を
再起動するときに、その起動トルクを小さくすることが
でき、圧縮機(4),(8)の作動信頼性を向上させる
ことができる。
In this embodiment, when the compressors (4) and (8) are stopped, the on-off valve (AV) is opened for a predetermined time to open the compressors (4) and (8) and the JT refrigerator (41). ) And the helium gas on the side of the compressors (4) and (8) is reduced, the helium gas on the side of the compressors (4) and (8) is then closed with the on-off valve (AV) closed. The pressure equalized when the helium gas in the refrigerant circuit (53) is equalized can be reduced. Therefore, when the compressors (4) and (8) are restarted in the pressure equalized state, the starting torque can be reduced, and the operational reliability of the compressors (4) and (8) is improved. be able to.

【0043】また、上記開閉弁(AV)は、液化槽(D
L )内の圧力が圧縮機(4),(8)側と同じ圧力で均
圧するのを防止するためにも使用されるので、この開閉
弁(AV)の機能の兼用化によってコストアップを招く
ことなく、上記効果が得られる。
The on-off valve (AV) is a liquefaction tank (D).
It is also used to prevent the pressure in L) from being equalized at the same pressure as the compressor (4), (8) side, so the dual use of the function of this on-off valve (AV) causes an increase in cost. Without the above, the above-mentioned effect can be obtained.

【0044】さらに、低圧配管(3)には逆止弁(C
V)が配設されているので、圧縮機(4),(8)の停
止時にはJ−T用高圧配管(15)(高圧配管(1
3))側の開閉弁(AV)を所定時間開いた後に閉じれ
ばよく、高圧配管(15)及び低圧配管(3)の双方を
それぞれ開閉弁で開閉制御する場合に比べ、開閉機構
(54)の構成を簡略にすることができる。
Further, the low-pressure pipe (3) has a check valve (C
V) is installed, the JT high-pressure pipe (15) (high-pressure pipe (1) when the compressors (4) and (8) are stopped.
The open / close valve (AV) on the side 3)) may be opened for a predetermined time and then closed, as compared with the case where both the high pressure pipe (15) and the low pressure pipe (3) are controlled to open / close by the open / close valve (54). The configuration of can be simplified.

【0045】また、開閉弁(AV)が空圧源(56)か
らの空気圧力により開閉する空圧弁で、空圧用電磁弁
(57)の切換動作により開閉制御されるので、開閉弁
(AV)が磁場中に配置されていても、その磁場の影響
を受けることなく開閉弁(AV)を安定して開閉動作さ
せることができる。
The on-off valve (AV) is an air-pressure valve which is opened and closed by the air pressure from the air-pressure source (56). Since the on-off valve is controlled by the switching operation of the solenoid valve for air pressure (57), the on-off valve (AV) is opened. Even if is placed in a magnetic field, the on-off valve (AV) can be stably opened and closed without being affected by the magnetic field.

【0046】(実施例2)図3は本発明の実施例2を示
し(尚、図1及び図2と同じ部分については同じ符号を
付してその詳細な説明は省略する)、上記実施例1で
は、開閉弁(AV)を空圧弁で構成しているのに対し、
制御装置(61)からの電気制御信号を受けてJ−T用
高圧配管(15)を開閉する電磁弁で構成したものであ
る。従って、この実施例でも、上記実施例1と同様の作
用効果を奏することができる。
(Embodiment 2) FIG. 3 shows Embodiment 2 of the present invention (note that the same parts as those in FIGS. 1 and 2 are designated by the same reference numerals and detailed description thereof will be omitted), In 1, the open / close valve (AV) is composed of a pneumatic valve, whereas
The solenoid valve is configured to open and close the JT high-pressure pipe (15) by receiving an electric control signal from the control device (61). Therefore, also in this embodiment, the same operational effect as that of the above-described first embodiment can be obtained.

【0047】[0047]

【発明の効果】以上説明したように、請求項1又は6の
発明によると、圧縮機と膨張手段とを高圧配管及び低圧
配管により接続した冷媒回路の一部を液化槽内に開放し
てなり、液化槽内で蒸発したガス冷媒を圧縮機に吸い込
んで圧縮し、この圧縮機で圧縮されたガス冷媒を膨張手
段で膨張させて液化し、この液冷媒を液化槽に戻すよう
にした極低温冷凍機において、圧縮機の停止時、その圧
縮機と膨張手段との間の冷媒回路を所定時間だけ開状態
に保持して圧縮機側のガス冷媒を膨張手段側に流し、圧
縮機側の冷媒回路におけるガス冷媒量を減少させるよう
にしたことにより、その圧縮機側の冷媒回路での均圧圧
力自体を低下させることができ、コストアップを抑制し
つつ、圧縮機の再起動時の起動トルクを小さくしてその
作動信頼性の向上を図ることができる。
As described above, according to the invention of claim 1 or 6, a part of the refrigerant circuit in which the compressor and the expansion means are connected by the high pressure pipe and the low pressure pipe is opened in the liquefaction tank. , A cryogenic temperature in which the gas refrigerant evaporated in the liquefaction tank is sucked into the compressor and compressed, and the gas refrigerant compressed by this compressor is expanded and liquefied by the expansion means and returned to the liquefaction tank In the refrigerator, when the compressor is stopped, the refrigerant circuit between the compressor and the expansion means is kept open for a predetermined time to allow the gas refrigerant on the compressor side to flow to the expansion means side and the refrigerant on the compressor side. By reducing the amount of gas refrigerant in the circuit, it is possible to reduce the pressure equalizing pressure itself in the refrigerant circuit on the compressor side, while suppressing the cost increase and starting torque when the compressor is restarted. Smaller to improve its operational reliability It is possible to achieve.

【0048】請求項2の発明によると、圧縮機の停止か
ら開閉手段を開くまでの時間は、液化槽内部の圧力が設
定圧力に上昇するまでの時間としたことにより、液化槽
内部の過大な圧力上昇を確実に防止することができる。
According to the second aspect of the invention, the time from the stop of the compressor to the opening of the opening / closing means is the time until the pressure inside the liquefaction tank rises to the set pressure, so that the inside of the liquefaction tank is excessive. It is possible to reliably prevent pressure increase.

【0049】請求項3の発明によると、開閉手段を、高
圧配管を開閉する開閉弁と、低圧配管に配設され、圧縮
機からガス冷媒が膨張手段に移動するのを阻止する逆止
弁とで構成したことにより、開閉手段の構成の簡略化を
図ることができる。
According to the third aspect of the invention, the opening / closing means includes an opening / closing valve for opening / closing the high pressure pipe, and a check valve arranged in the low pressure pipe for preventing the gas refrigerant from moving from the compressor to the expansion means. With this configuration, the structure of the opening / closing means can be simplified.

【0050】請求項4の発明では、開閉弁は電磁弁と
し、請求項5の発明では、開閉弁は空圧弁とした。これ
ら発明によると、開閉弁の具体的構成が得られる。特
に、請求項5の発明によると、開閉弁としての空圧弁は
空気圧力により開閉するので、磁場等の影響を受けるこ
となく安定して冷媒回路を開閉することができる。
In the invention of claim 4, the on-off valve is an electromagnetic valve, and in the invention of claim 5, the on-off valve is a pneumatic valve. According to these inventions, a specific configuration of the on-off valve can be obtained. In particular, according to the fifth aspect of the invention, since the pneumatic valve as the on-off valve is opened and closed by the air pressure, the refrigerant circuit can be stably opened and closed without being affected by the magnetic field or the like.

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

【図1】本発明の実施例1における要部の構成を示す図
である。
FIG. 1 is a diagram showing a configuration of a main part in a first embodiment of the present invention.

【図2】本発明の実施例1における冷凍機の全体構成を
示す冷媒回路図である。
FIG. 2 is a refrigerant circuit diagram showing the overall configuration of the refrigerator in the first embodiment of the present invention.

【図3】本発明の実施例2を示す図1相当図である。FIG. 3 is a view corresponding to FIG. 1 and showing a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

(R) 冷凍機 (1) 圧縮機ユニット (3) 低圧配管 (4),(8) 圧縮機 (13) 高圧配管 (15) J−T用高圧配管 (31) 冷凍機ユニット (32) 予冷冷凍機 (41) J−T冷凍機(膨張手段) (48) J−T弁 (53) 冷媒回路 (AV) 開閉弁 (CV) 逆止弁 (54) 開閉機構(開閉手段) (57) 空圧用電磁弁 (61) 制御装置(制御手段) (DL ) 液化槽 (R) Refrigerator (1) Compressor unit (3) Low pressure piping (4), (8) Compressor (13) High pressure piping (15) JT high pressure piping (31) Refrigerator unit (32) Pre-cooled refrigeration Machine (41) JT refrigerator (expansion means) (48) JT valve (53) Refrigerant circuit (AV) Open / close valve (CV) Check valve (54) Open / close mechanism (open / close means) (57) For pneumatic pressure Solenoid valve (61) Control device (control means) (DL) Liquefaction tank

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 ヘリウムガス等の冷媒ガスを圧縮する圧
縮機(4),(8)と、高圧のガス冷媒を膨張させて寒
冷を発生させる膨張手段(41)とを高圧配管(15)
及び低圧配管(3)により接続してなる冷媒回路(5
3)と、 内部に上記冷媒回路(53)の一部が開放され、液冷媒
を溜める液化槽(DL)とを備え、 液化槽(DL )内で蒸発したガス冷媒を冷媒回路(5
3)に吸入して圧縮機(4),(8)で圧縮するととも
に、この圧縮されたガス冷媒を膨張手段(41)で膨張
させ、その膨張による温度降下により液冷媒を生成して
液化槽(DL )内に戻すようにした極低温冷凍機におい
て、 上記圧縮機(4),(8)と膨張手段(41)とを連通
又は連通遮断する開閉手段(54)と、 圧縮機(4),(8)の停止から所定時間が経過するま
での間は上記開閉手段(54)を開き、所定時間の経過
後に上記開閉手段(54)を閉じるように制御する制御
手段(61)とを設けたことを特徴とする極低温冷凍機
の均圧制御装置。
1. High-pressure pipe (15) comprising compressors (4), (8) for compressing a refrigerant gas such as helium gas and an expansion means (41) for expanding a high-pressure gas refrigerant to generate cold.
And a refrigerant circuit (5 connected by low pressure piping (3)
3) and a liquefaction tank (DL) in which a part of the refrigerant circuit (53) is opened to store the liquid refrigerant. The gas refrigerant evaporated in the liquefaction tank (DL) is supplied to the refrigerant circuit (5).
3) is sucked into and compressed by the compressors (4) and (8), and the compressed gas refrigerant is expanded by the expansion means (41), and the liquid refrigerant is generated by the temperature drop due to the expansion and the liquefaction tank. In a cryogenic refrigerator which is returned to (DL), an opening / closing means (54) for connecting or disconnecting the compressors (4), (8) and the expansion means (41), and a compressor (4) , (8) from the stop of the opening and closing of the opening and closing means (54) until a predetermined time has elapsed, and a control means (61) for controlling the opening and closing means (54) to close after the elapse of a predetermined time. A pressure equalizing controller for a cryogenic refrigerator.
【請求項2】 請求項1記載の極低温冷凍機の均圧制御
装置において、 制御手段(61)が圧縮機(4),(8)の停止後に開
閉手段(54)を開く時間は、液化槽(DL )内部の圧
力が設定圧力に上昇するまでの時間であることを特徴と
する極低温冷凍機の均圧制御装置。
2. The pressure equalizing control device for a cryogenic refrigerator according to claim 1, wherein the control means (61) opens the opening / closing means (54) after stopping the compressors (4), (8), and is liquefied. A pressure equalization control device for a cryogenic refrigerator, which is the time until the pressure inside the tank (DL) rises to a set pressure.
【請求項3】 請求項1又は2記載の極低温冷凍機の均
圧制御装置において、 開閉手段(54)は、高圧配管(15)を開閉する開閉
弁(AV)と、 低圧配管(3)に配設され、膨張手段(41)のガス冷
媒が圧縮機(4),(8)に戻るのは許容する一方、圧
縮機(4),(8)からガス冷媒が膨張手段(41)に
移動するのは阻止する逆止弁(CV)とで構成されてい
ることを特徴とする極低温冷凍機の均圧制御装置。
3. The pressure equalizing control device for a cryogenic refrigerator according to claim 1, wherein the opening / closing means (54) opens and closes the high pressure pipe (15), and the low pressure pipe (3). And permits the gas refrigerant of the expansion means (41) to return to the compressors (4) and (8), while the gas refrigerant from the compressors (4) and (8) flows to the expansion means (41). A pressure equalizing control device for a cryogenic refrigerator, which is configured with a check valve (CV) that blocks movement.
【請求項4】 請求項3記載の極低温冷凍機の均圧制御
装置において、 開閉弁(AV)は電磁弁であることを特徴とする極低温
冷凍機の均圧制御装置。
4. The pressure equalizing control device for a cryogenic refrigerator according to claim 3, wherein the on-off valve (AV) is a solenoid valve.
【請求項5】 請求項3記載の極低温冷凍機の均圧制御
装置において、 開閉弁(AV)は、空気圧力により開閉する空圧弁であ
ることを特徴とする極低温冷凍機の均圧制御装置。
5. The pressure equalizing control device for a cryogenic refrigerator according to claim 3, wherein the on-off valve (AV) is a pneumatic valve that opens and closes by air pressure. apparatus.
【請求項6】 ヘリウムガス等のガス冷媒を圧縮する圧
縮機(4),(8)と、高圧のガス冷媒を膨張させて寒
冷を発生させる膨張手段(41)とを高圧配管(15)
及び低圧配管(3)により接続してなる冷媒回路(5
3)と、 内部に上記冷媒回路(53)の一部が開放され、液冷媒
を溜める液化槽(DL)とを備え、 液化槽(DL )内で蒸発したガス冷媒を冷媒回路(5
3)に吸入して圧縮機(4),(8)で圧縮するととも
に、この圧縮されたガス冷媒を膨張手段(41)で膨張
させ、その膨張による温度降下により液冷媒を生成して
液化槽(DL )内に戻すようにした極低温冷凍機におい
て、 上記圧縮機(4),(8)の停止から所定時間が経過す
るまでの間は圧縮機(4),(8)と膨張手段(41)
とを連通させ、 上記所定時間の経過後に圧縮機(4),(8)と膨張手
段(41)との連通を遮断することを特徴とする極低温
冷凍機の均圧制御方法。
6. High-pressure pipe (15) comprising compressors (4), (8) for compressing a gas refrigerant such as helium gas, and expansion means (41) for expanding the high-pressure gas refrigerant to generate cold.
And a refrigerant circuit (5 connected by low pressure piping (3)
3) and a liquefaction tank (DL) in which a part of the refrigerant circuit (53) is opened to store the liquid refrigerant. The gas refrigerant evaporated in the liquefaction tank (DL) is supplied to the refrigerant circuit (5).
3) is sucked into and compressed by the compressors (4) and (8), and the compressed gas refrigerant is expanded by the expansion means (41), and the liquid refrigerant is generated by the temperature drop due to the expansion and the liquefaction tank. In the cryogenic refrigerator which is returned to the inside of (DL), the compressors (4) and (8) and the expansion means (from the stop of the compressors (4) and (8) until a predetermined time elapses. 41)
And the communication between the compressors (4), (8) and the expansion means (41) is cut off after the lapse of the predetermined time, and a pressure equalization control method for a cryogenic refrigerator.
JP12342495A 1995-05-23 1995-05-23 Equalization control method and equalization control device for cryogenic refrigerator Expired - Fee Related JP2725631B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12342495A JP2725631B2 (en) 1995-05-23 1995-05-23 Equalization control method and equalization control device for cryogenic refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12342495A JP2725631B2 (en) 1995-05-23 1995-05-23 Equalization control method and equalization control device for cryogenic refrigerator

Publications (2)

Publication Number Publication Date
JPH08313085A true JPH08313085A (en) 1996-11-29
JP2725631B2 JP2725631B2 (en) 1998-03-11

Family

ID=14860223

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12342495A Expired - Fee Related JP2725631B2 (en) 1995-05-23 1995-05-23 Equalization control method and equalization control device for cryogenic refrigerator

Country Status (1)

Country Link
JP (1) JP2725631B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009066565A1 (en) * 2007-11-19 2009-05-28 Ihi Corporation Cryogenic refrigerator and control method therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009066565A1 (en) * 2007-11-19 2009-05-28 Ihi Corporation Cryogenic refrigerator and control method therefor

Also Published As

Publication number Publication date
JP2725631B2 (en) 1998-03-11

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