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JPH0349024B2 - - Google Patents
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JPH0349024B2 - - Google Patents

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Publication number
JPH0349024B2
JPH0349024B2 JP5831684A JP5831684A JPH0349024B2 JP H0349024 B2 JPH0349024 B2 JP H0349024B2 JP 5831684 A JP5831684 A JP 5831684A JP 5831684 A JP5831684 A JP 5831684A JP H0349024 B2 JPH0349024 B2 JP H0349024B2
Authority
JP
Japan
Prior art keywords
pressure
line
valve
expander
cryogenic
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.)
Expired
Application number
JP5831684A
Other languages
Japanese (ja)
Other versions
JPS60205158A (en
Inventor
Kozo Matsumoto
Hirotake Kajiwara
Ikuo Kawamura
Norimoto Matsuda
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.)
Hitachi Ltd
Original Assignee
Hitachi Techno Engineering Co Ltd
Hitachi 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 Hitachi Techno Engineering Co Ltd, Hitachi Ltd filed Critical Hitachi Techno Engineering Co Ltd
Priority to JP5831684A priority Critical patent/JPS60205158A/en
Publication of JPS60205158A publication Critical patent/JPS60205158A/en
Publication of JPH0349024B2 publication Critical patent/JPH0349024B2/ja
Granted legal-status Critical Current

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  • Separation By Low-Temperature Treatments (AREA)
  • Containers, Films, And Cooling For Superconductive Devices (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔発明の利用分野〕 本発明は、極低温冷凍機に係り、特に多様な負
荷条件を要求せず長期連続運転が必要な極低温冷
凍機に関するものである。 〔発明の背景〕 ヘリウム冷凍機等の極低温冷凍機は、常温から
の予冷に長時間を要し、このために過渡的な運転
制御に特別な対策がなされている。また、定常運
転時には、被冷却体側の負荷に合わせた制御を行
うための機構が考えられている。以下、極低温冷
凍機としてヘリウム冷凍機を例として第1図によ
り従来の極低温冷凍機を説明する。 第1図で、ヘリウム冷凍機10は、真空排気さ
れる保冷槽11と熱交換器12a〜12eと膨張
機13a,13bとで主に構成されている。保冷
槽11内には、熱交換器12a〜12eが第1図
では上側から下側へ順次配設され、高圧ライン1
4が熱交換器12a〜12eの各高圧流路を連通
して設けられ、低圧ライン15が熱交換器12a
〜12eの各低圧流路を連通して設けられてい
る。熱交換器12aと熱交換器12bとの間の高
圧ライン14からは膨張機ライン16が分岐さ
れ、熱交換機12cの中圧流路を介してその分岐
端は熱交換器12d,12e間の低圧ライン15
に連結されている。熱交換器12d,12e間の
高圧ライン14からバイパスライン17が分岐
し、バイパスライン17の分岐端は熱交換器12
e前流側の低圧ライン15に連結されている。膨
張機ライン16の熱交換器12cの前流側には膨
張機入口弁18が設けられ膨張機入口弁18と熱
交換器12cとの間の膨張機ライン16には膨張
機13aが設けられている。熱交換器12cの後
流側の膨張機ライン16には膨張機13bが設け
られている。バイパスライン17には、予冷弁1
9が設けられ、高圧ライン14の冷媒出口端(第
1図では、下端)には、ジユール、トムソン膨張
弁(以下、JT弁と略)20が設けられている。
圧縮機30は、保冷槽11外に配置され、その吐
出端には配管31の一端が、その吸入端には配管
32の一端が連結されている。配管31の他端
は、高圧ライン14の冷媒入口端(第1図では、
上端)に連結され、配管32の他端は、低圧ライ
ン15の冷媒出口端(第1図では、上端)に連結
されている。また、保冷槽11外には、中圧タン
ク40が配置され中圧タンク40と配管31,3
2とは、それぞれ配管41,42で連結され、配
管41,42には、圧力調整弁43a,43bが
それぞれ設けられている。保冷槽11と真空連通
するクライオスタツト50のクライオスタツト内
槽(以下、クライオ内槽と略)51には被冷却体
52が内蔵されている。JT弁20の出口端には、
冷媒供給ライン21の一端が連結され、その他端
はクライオ内槽51に連通されている。低圧ライ
ン15の冷媒入口端(第1図では、下端)はクラ
イオ内槽51にガス層と連通して連結されてい
る。 第1図で、圧縮機30で圧縮され昇圧された高
圧ベリウムガス(以下、高圧GHeと略)は、配
管31を経て高圧ライン14に導入され、熱交換
器12aの高圧流路に供給される。この高圧流路
を流通する間に高圧GHeは、熱交換器12aの
低圧流路を流通する低圧ヘリウムガス(以下、低
圧GHeと略)と熱交換して冷却された後に熱交
換器12aの高圧流路より排出される。この排出
された高圧GHeは膨張機ライン16に一部分流
される。分流された高圧GHeは、膨張機入口弁
18を通り膨張機13aで断熱膨張仕事を行い寒
冷を発生した後、熱交換器12cでその低圧流路
を流通する低圧GHeと熱交換し、その後、膨張
機13bで再び断熱膨張仕事を行い寒冷を発生し
熱交換器12d,12e間の低圧ライン15を流
通する低圧GHeと合流される。一方、残りの高
圧GHeは、熱交換器12a〜12eで低圧GHe
と熱交換し順次冷却された後JT弁20でジユー
ル・トムソン膨張し液化される。液化されたヘリ
ウムガス(以下、LHeと略)は冷媒供給ライン
21を経てクライオ槽51に供給され、この
LHeにより被冷却体52は浸漬される。クライ
オ内槽51のLHeはクライオスタツト50の被
冷却体52を含む冷凍負荷吸収により一部蒸発し
低圧GHeとなり、この低圧GHeは、熱交換器1
2e〜12aで高圧GHeとそれぞれ熱交換する
ことによつて寒冷を回収された後に圧縮機30に
戻される。 次に各弁の基本的機能について説明する。 (1) 膨張入口弁18 第1の機能は、膨張機13a,13bの負荷
制御機能である。膨張機13a,13bには、
ヘリウムガス(以下、GHeと略)の断熱膨張
仕事を吸収するための制御装置(図示省略)が
付属しているが、しかし、その制御範囲は広く
ない。これに対し、断熱膨張仕事による負荷
は、膨張比が同じであれば入口GHe温度に比
例して増大する。したがつて、ヘリウム冷凍機
10の起動時には、制御装置で制御不可能な負
荷がかかることがあり得る。このため、ヘリウ
ム冷凍機10の起動時には、膨張機入口弁18
を絞り膨張機13a,13bでの膨張比を小さ
くして負荷を制御する必要がある。第2の機能
は、定常運転時にクライオスタツト50の負荷
条件に合わせたヘリウム冷凍機10の運転制御
である。即ち、クライオスタツト50の負荷条
件が、冷凍負荷だけの場合と他の、例えば、液
化負荷の場合とでは、膨張機ライン16に分流
すべき高圧GHeの流量割合いは大きく異なる。
膨張機入口弁18は、このような負荷条件に対
応したヘリウム冷凍機10の運転制御に使用さ
れる。 (2) JT弁20 JT弁20は、ヘリウム冷凍機10の能力調
整用として基本的には使用される。 (3) 予冷弁19 予冷弁19は、ヘリウム冷凍機10の予冷運
転時のバイパス用に使用される。即ち、熱交換
器12eが高性能で、また、JT弁20は定常
運転時の使用条件に合わせて設計されているた
め、予冷運転時にはGHeを少量しか流せず予
冷に長時間を要することになる。そこで、この
予冷運転時間を短縮するために、予冷運転時に
は、予冷弁19によつて熱交換器12eをバイ
パスできるようにしている。 (4) 圧力調整弁43a,43b 圧力調整弁43a,43bは中圧タンク40
をバツフアーとして高圧GHeおよび低圧GHe
の圧力制御を行う。 このような極低温冷凍機では、膨張機入口弁、
JT弁、予冷弁といつた高価な極低温弁を使用し、
また、これにより保冷槽内の極低温配管が複雑に
なるため、その価格が増大するといつた欠点があ
つた。また、極低温弁は比較的その信頼性が低い
ため、これにより極低温冷凍機の信頼性が低下す
るといつた欠点もあつた。また、極低温弁の操作
部を保冷槽外に出しておく必要があるため、操作
部から保冷槽内への熱浸入が生じ、これにより極
低温冷凍機の性能が低下するといつた欠点もあつ
た。また、運転時の操作部が多いため、極低温冷
凍機の運転操作が難しくなるとつた欠点もあつ
た。 〔発明の目的〕 本発明の目的は、高価な極低温弁を不用にする
ことで、価格を低減できる極低温冷凍機を提供す
ることにある。 〔発明の概要〕 本発明は、真空排気される保冷槽内に複数個の
熱交換器を配設し、保冷槽内で熱交換器の高圧流
路と連通する高圧ラインより分岐し熱交換器の低
圧流路と連通する低圧ラインと合流した膨張機ラ
インに膨張機を設け、高圧ラインの冷媒出口端に
固定絞り手段を設け、高圧ラインの冷媒入口端側
で、かつ、保冷槽外に冷媒圧力調整手段を設けた
ことを特徴とするもので、高価な極低温弁を不用
にしたものである。 〔発明の実施例〕 従来の極低温冷凍機で使用されている極低温弁
の基本的機能は上記したとおりであり、液化運転
もあり冷凍運転もあり、また、起動、停止を頻繁
に行うような極低温冷凍機では、極低温弁はおの
おのそれなりの意味、効果を有する。しかしなが
ら、運転として、例えば、冷凍運転が主であり、
多様な負荷条件を要求せず、長期連続運転が必要
な極低温冷凍機では、基本的再検討が可能であ
る。 そこで、このような極低温冷凍機について鋭意
検討を行つた結果、極低温弁の内で膨張機入口弁
については、予冷時の膨張機の負荷制御は、高圧
ラインに導入する高圧冷媒ガスの圧力を変化させ
ることで行えば良く、また、定常時の運転モード
は主たる運転条件に合わせ膨張機を設計しておけ
ば良く、膨張機ラインに分流される冷媒ガスの流
量制御の必要は無くなるという知見を得、また、
JT弁は、固定の絞り手段であれば良く、冷凍能
力の調節は、高圧ラインに導入される高圧冷媒ガ
スの圧力調整によつて容易に行えるという知見を
得た。なお、予冷弁は、予冷時間の短縮にその使
用目的があり、このような極低温冷凍機では、予
冷時間は差程大きな問題ではなく不用にできる。 以下、本発明の一実施例を第2図〜第4図によ
り説明する。この場合、極低温冷凍機はヘリウム
冷凍機である。 第2図で、高圧ライン14の冷媒出口端(第2
図では、下端)には、従来のJT弁に代り固定絞
り手段、例えば、第3図に示すようなオリフイス
式の固定絞り手段60が設けられている。固定絞
り手段60は、高圧ライン14に設けたフランジ
61と冷媒供給ライン21に設けたフランジ62
とでオリフイス63を固定した構造のものであ
る。また、この場合、冷媒圧力調整手段は特別に
設けず、高圧ライン14の冷媒入口端側で、か
つ、保冷槽11外に設けられている圧力長成分4
32を圧力調整手段として共用している。また、
第1図で示したバイパスライン、膨張機入口弁、
予冷弁通はそれぞれ除去されている。なお、第2
図で、その他第1図と同一装置、部品等は同一符
号で示し説明を省略する。 第2図で、ヘリウム冷凍機10の定常運転時の
冷凍能力の制御は、高圧ライン14に導入される
高圧GHeの圧力を調整することによつて行う。
即ち、圧力調整弁43aの設定値を冷凍負荷に合
わせて調整する。ヘリウム冷凍機10が、多様な
負荷条件を要求せず長期連続運転が必要なヘリウ
ム冷凍機である場合、高圧ライン14に導入され
る高圧GHeの圧力Pと冷凍能力Qとの間には、
第4図に示すようにほぼ直線関係が成り立つ。こ
れにより、ヘリウム冷凍機10の定常運転時の冷
凍能力の制御は、高圧ライン14に導入される高
圧GHeの圧力を圧力調整弁43aで調整するこ
とで容易に行うことができる。なお、第4図での
高圧ライン14に導入される高圧GHeの圧力P
とは、式(1)で表わされるもので、冷凍能力Qと
は、式(2)で表わされるものである。 P=高圧ライン入口圧力/圧縮機の吐出圧力×100(
%)……(1) Q=実働冷凍能力/設計冷凍能力×100(%)…
…(2) 次に、予冷運転時の膨張機13a,13bの制
動負荷の制御は、上記した定常運転時の冷凍能力
の制御と同様に、高圧ライン14に導入される高
圧GHeの圧力を圧力調整弁43aで調整するこ
で行うことができる。 本実施例のような冷凍機では、次のような効果
を得ることができる。 (1) 高価な極低温弁が不用で、また、これにより
保冷槽内の極低温配管を簡略化できるため、ヘ
リウム冷凍機の価格を低減できる。 (2) 比較的信頼性が低い極低温弁が不用であるた
め、ヘリウム冷凍機の信頼性を向上できる。 (3) 極低温弁が不用で、これにより操作部も不用
となるため、保冷槽内への熱侵入を防止でき、
これによるヘリウム冷凍機の性能低下を防止で
きる。 (4) 運転時の操作部を大幅に減少できヘリウム冷
凍機の運転操作が極めて簡易になる。 なお、本実施例の他に、高圧ラインの冷媒入口
端側で、かつ、保冷槽外にあり、圧縮機の吐出端
と高圧ラインの入口端とを連結する配管に圧力調
整弁等の圧力手段を設け、該圧力調整手段で高圧
ラインに導入される高圧GHeの圧力を調整する
ようにしても良く、また、圧縮機自体に圧力調整
手段の機能を具備させて直接圧力調整するように
しても良い。また、直接的には高圧ラインに導入
される高圧GHeの流量調整により高圧ラインに
導入される高圧GHeの圧力を調整するようにし
ても良い。また、本実施例では、JT弁に代る固
定絞り手段を保冷槽内に設けているが、高圧ライ
ンの冷媒出口端であれば、この他にクライオスタ
ツタ内に設けても、また、ヘリウム冷凍機とクラ
イオスタツトとが極低温移送配管で連結されてい
る場合には、極低温移送配管の途中に設けても良
い。まだ、JT弁に代る固定絞り手段としては、
本実施例の他にベンチユリ式の固定絞り手段のよ
うに運転中に開度が変えられないものであれば問
題なく適用できる。 〔発明の効果〕 本発明は、真空排気される保冷槽内に複数個の
熱交換器を配設し、保冷槽内で熱交換器の高圧流
路と連通する高圧ラインより分岐し熱交換器の低
圧流路と連通する低圧ラインに合流した膨張機ラ
インに膨張機を設け、高圧ラインの冷媒出口端に
固定絞り手段を設け、高圧ラインの冷媒入口端側
で、かつ、保冷槽外に冷媒圧力調整手段を設けた
ことで、高価な極低温弁が不用で、また、これに
より保冷槽内の極低温配管を簡略化できるので、
極低温冷凍機の価格を低減できるという効果があ
る。
[Field of Application of the Invention] The present invention relates to a cryogenic refrigerator, and particularly to a cryogenic refrigerator that does not require various load conditions and requires long-term continuous operation. [Background of the Invention] Cryogenic refrigerators such as helium refrigerators require a long time to precool from room temperature, and therefore special measures are taken for transient operation control. Additionally, mechanisms have been devised to perform control in accordance with the load on the object to be cooled during steady operation. Hereinafter, a conventional cryogenic refrigerator will be explained with reference to FIG. 1, taking a helium refrigerator as an example of the cryogenic refrigerator. In FIG. 1, a helium refrigerator 10 mainly includes a cold storage tank 11 that is evacuated, heat exchangers 12a to 12e, and expanders 13a and 13b. In the cold storage tank 11, heat exchangers 12a to 12e are sequentially arranged from the top to the bottom in FIG.
4 is provided to communicate each high pressure flow path of the heat exchangers 12a to 12e, and a low pressure line 15 is provided to communicate with each high pressure flow path of the heat exchangers 12a to 12e.
~12e are provided in communication with each of the low pressure channels. An expander line 16 is branched from the high pressure line 14 between the heat exchanger 12a and the heat exchanger 12b, and the branched end is connected to the low pressure line between the heat exchangers 12d and 12e via the medium pressure flow path of the heat exchanger 12c. 15
is connected to. A bypass line 17 branches from the high pressure line 14 between the heat exchangers 12d and 12e, and the branched end of the bypass line 17 is connected to the heat exchanger 12.
e Connected to the low pressure line 15 on the upstream side. An expander inlet valve 18 is provided on the upstream side of the heat exchanger 12c in the expander line 16, and an expander 13a is provided in the expander line 16 between the expander inlet valve 18 and the heat exchanger 12c. There is. An expander 13b is provided in the expander line 16 on the downstream side of the heat exchanger 12c. The bypass line 17 includes a pre-cooling valve 1.
9, and a Jul-Thomson expansion valve (hereinafter abbreviated as JT valve) 20 is provided at the refrigerant outlet end (lower end in FIG. 1) of the high pressure line 14.
The compressor 30 is arranged outside the cold storage tank 11, and its discharge end is connected to one end of a pipe 31, and its suction end is connected to one end of a pipe 32. The other end of the pipe 31 is the refrigerant inlet end of the high pressure line 14 (in FIG.
The other end of the pipe 32 is connected to the refrigerant outlet end (the upper end in FIG. 1) of the low pressure line 15. Further, a medium pressure tank 40 is arranged outside the cold storage tank 11, and the medium pressure tank 40 and the pipes 31, 3
2 are connected by pipes 41 and 42, respectively, and pressure regulating valves 43a and 43b are provided in the pipes 41 and 42, respectively. A cryostat inner tank (hereinafter abbreviated as cryo inner tank) 51 of the cryostat 50 which is in vacuum communication with the cold storage tank 11 has a cooled body 52 built therein. At the outlet end of the JT valve 20,
One end of the refrigerant supply line 21 is connected, and the other end is communicated with the cryo inner tank 51. The refrigerant inlet end (lower end in FIG. 1) of the low pressure line 15 is connected to the cryo inner tank 51 in communication with the gas layer. In FIG. 1, high-pressure beryum gas (hereinafter abbreviated as high-pressure GHe) compressed and pressurized by a compressor 30 is introduced into a high-pressure line 14 through a pipe 31, and is supplied to a high-pressure flow path of a heat exchanger 12a. While flowing through this high-pressure flow path, the high-pressure GHe is cooled by exchanging heat with low-pressure helium gas (hereinafter abbreviated as low-pressure GHe) flowing through the low-pressure flow path of the heat exchanger 12a. It is discharged from the flow path. A portion of this discharged high pressure GHe is flowed into the expander line 16. The divided high-pressure GHe passes through the expander inlet valve 18 and performs adiabatic expansion work in the expander 13a to generate cold, and then exchanges heat with the low-pressure GHe flowing through the low-pressure flow path in the heat exchanger 12c, and then, The expander 13b performs adiabatic expansion work again to generate cold, which is merged with low-pressure GHe flowing through the low-pressure line 15 between the heat exchangers 12d and 12e. On the other hand, the remaining high-pressure GHe is transferred to the low-pressure GHe in the heat exchangers 12a to 12e.
After being sequentially cooled by heat exchange with JT valve 20, it is expanded and liquefied. Liquefied helium gas (hereinafter abbreviated as LHe) is supplied to the cryo tank 51 via the refrigerant supply line 21.
The object to be cooled 52 is immersed in LHe. LHe in the cryo inner tank 51 partially evaporates into low pressure GHe due to absorption of the refrigeration load including the cooled body 52 of the cryostat 50, and this low pressure GHe is transferred to the heat exchanger 1.
The cold is recovered by heat exchange with high-pressure GHe in 2e to 12a, and then returned to the compressor 30. Next, the basic functions of each valve will be explained. (1) Expansion inlet valve 18 The first function is a load control function of the expanders 13a and 13b. The expanders 13a and 13b include
A control device (not shown) is attached to absorb the work of adiabatic expansion of helium gas (hereinafter abbreviated as GHe), but its control range is not wide. On the other hand, the load due to adiabatic expansion work increases in proportion to the inlet GHe temperature if the expansion ratio remains the same. Therefore, when starting up the helium refrigerator 10, a load that cannot be controlled by the control device may be applied. Therefore, when starting the helium refrigerator 10, the expander inlet valve 18
It is necessary to control the load by reducing the expansion ratio in the expanders 13a and 13b. The second function is to control the operation of the helium refrigerator 10 in accordance with the load conditions of the cryostat 50 during steady operation. That is, the flow rate ratio of high-pressure GHe to be diverted to the expander line 16 differs greatly between when the load condition of the cryostat 50 is only a refrigeration load and when it is other, for example, a liquefaction load.
The expander inlet valve 18 is used to control the operation of the helium refrigerator 10 in response to such load conditions. (2) JT valve 20 The JT valve 20 is basically used to adjust the capacity of the helium refrigerator 10. (3) Precooling valve 19 The precooling valve 19 is used for bypass during precooling operation of the helium refrigerator 10. That is, since the heat exchanger 12e has high performance and the JT valve 20 is designed to suit the usage conditions during steady operation, only a small amount of GHe can flow during precooling operation, and precooling takes a long time. . Therefore, in order to shorten this precooling operation time, the heat exchanger 12e can be bypassed by the precooling valve 19 during the precooling operation. (4) Pressure adjustment valves 43a, 43b Pressure adjustment valves 43a, 43b are intermediate pressure tank 40
High pressure GHe and low pressure GHe as a buffer
Performs pressure control. In such cryogenic refrigerators, the expander inlet valve,
Using expensive cryogenic valves such as JT valves and pre-cooling valves,
In addition, this made the cryogenic piping inside the cold storage tank complicated, resulting in an increase in cost. Another disadvantage was that the reliability of the cryogenic valve was relatively low, thereby reducing the reliability of the cryogenic refrigerator. In addition, because the operation part of the cryogenic valve needs to be placed outside the cold storage tank, heat leaks from the operation part into the cold storage tank, which has the disadvantage of reducing the performance of the cryogenic refrigerator. Ta. Another drawback was that it became difficult to operate the cryogenic refrigerator due to the large number of operation parts during operation. [Object of the Invention] An object of the present invention is to provide a cryogenic refrigerator that can reduce the cost by eliminating the need for an expensive cryogenic valve. [Summary of the Invention] The present invention provides a heat exchanger system in which a plurality of heat exchangers are arranged in a cold storage tank that is evacuated, and a high-pressure line that communicates with a high-pressure flow path of the heat exchanger branches within the cold storage tank. An expander is installed in the expander line that merges with the low pressure line that communicates with the low pressure flow path of It is characterized by the provision of a pressure regulating means, which eliminates the need for an expensive cryogenic valve. [Embodiment of the Invention] The basic functions of cryogenic valves used in conventional cryogenic refrigerators are as described above. In a cryogenic refrigerator, each cryogenic valve has its own meaning and effect. However, the main operation is, for example, refrigeration operation,
For cryogenic refrigerators that do not require diverse load conditions and require long-term continuous operation, a fundamental reconsideration is possible. Therefore, as a result of intensive study on such cryogenic refrigerators, we found that among the cryogenic valves, the expander inlet valve controls the load of the expander during precooling by adjusting the pressure of the high-pressure refrigerant gas introduced into the high-pressure line. The knowledge that this can be done by changing the flow rate of the refrigerant gas divided into the expander line is eliminated, as the expansion machine can be designed in accordance with the main operating conditions for the steady-state operation mode. and also
It was found that the JT valve only needs to be a fixed throttle means, and that the refrigerating capacity can be easily adjusted by adjusting the pressure of the high-pressure refrigerant gas introduced into the high-pressure line. Note that the purpose of the precooling valve is to shorten the precooling time, and in such a cryogenic refrigerator, the precooling time is not a big problem and can be omitted. An embodiment of the present invention will be described below with reference to FIGS. 2 to 4. In this case, the cryogenic refrigerator is a helium refrigerator. In FIG. 2, the refrigerant outlet end (second
At the lower end in the figure, a fixed throttle means, for example, an orifice-type fixed throttle means 60 as shown in FIG. 3, is provided in place of the conventional JT valve. The fixed throttle means 60 includes a flange 61 provided on the high pressure line 14 and a flange 62 provided on the refrigerant supply line 21.
It has a structure in which the orifice 63 is fixed with. In this case, no special refrigerant pressure adjustment means is provided, and the pressure length component 4 is provided on the refrigerant inlet end side of the high pressure line 14 and outside the cold storage tank 11.
32 is commonly used as pressure adjustment means. Also,
Bypass line shown in Figure 1, expander inlet valve,
Each pre-cooling valve passage has been removed. In addition, the second
In the figure, other devices, parts, etc. that are the same as those in FIG. In FIG. 2, the refrigerating capacity of the helium refrigerator 10 during steady operation is controlled by adjusting the pressure of high-pressure GHe introduced into the high-pressure line 14.
That is, the set value of the pressure regulating valve 43a is adjusted according to the refrigeration load. When the helium refrigerator 10 is a helium refrigerator that does not require various load conditions and requires long-term continuous operation, there is a difference between the pressure P of the high pressure GHe introduced into the high pressure line 14 and the refrigeration capacity Q.
As shown in FIG. 4, an almost linear relationship holds true. Thereby, the refrigerating capacity of the helium refrigerator 10 during steady operation can be easily controlled by adjusting the pressure of the high-pressure GHe introduced into the high-pressure line 14 using the pressure regulating valve 43a. In addition, the pressure P of the high pressure GHe introduced into the high pressure line 14 in FIG.
is expressed by equation (1), and refrigeration capacity Q is expressed by equation (2). P = High pressure line inlet pressure / Compressor discharge pressure x 100 (
%)...(1) Q = Actual refrigeration capacity/Design refrigeration capacity x 100 (%)...
...(2) Next, to control the braking load of the expanders 13a and 13b during pre-cooling operation, the pressure of the high-pressure GHe introduced into the high-pressure line 14 is adjusted to This can be done by adjusting with the regulating valve 43a. With the refrigerator as in this embodiment, the following effects can be obtained. (1) An expensive cryogenic valve is not required, and the cryogenic piping inside the cold storage tank can be simplified, so the price of the helium refrigerator can be reduced. (2) Since a cryogenic valve, which is relatively unreliable, is not required, the reliability of the helium refrigerator can be improved. (3) There is no need for a cryogenic valve, which also eliminates the need for an operating section, which prevents heat from entering the cold storage tank.
This can prevent performance deterioration of the helium refrigerator. (4) The number of operating parts during operation can be greatly reduced, making the operation of the helium refrigerator extremely simple. In addition to this embodiment, pressure means such as a pressure regulating valve may be installed on the piping that is located on the refrigerant inlet end side of the high pressure line and outside the cold storage tank and connects the discharge end of the compressor and the inlet end of the high pressure line. The pressure adjusting means may be provided to adjust the pressure of the high pressure GHe introduced into the high pressure line, or the compressor itself may be equipped with the function of a pressure adjusting means to directly adjust the pressure. good. Alternatively, the pressure of the high-pressure GHe introduced into the high-pressure line may be directly adjusted by adjusting the flow rate of the high-pressure GHe introduced into the high-pressure line. In addition, in this embodiment, a fixed throttle means is installed in the cold storage tank in place of the JT valve, but if it is at the refrigerant outlet end of the high-pressure line, it can also be installed inside the cryostat. If the cryostat and the cryostat are connected by a cryotransfer pipe, it may be provided in the middle of the cryotransfer pipe. As a fixed throttle means to replace the JT valve,
In addition to this embodiment, any device whose opening degree cannot be changed during operation, such as a bench lily type fixed throttle means, can be applied without any problem. [Effects of the Invention] The present invention provides a heat exchanger system in which a plurality of heat exchangers are arranged in a cold storage tank that is evacuated, and a high pressure line that communicates with a high pressure flow path of the heat exchanger branches out from a high pressure line that communicates with a high pressure flow path of the heat exchanger. An expander is installed in the expander line that joins the low pressure line that communicates with the low pressure flow path of By providing a pressure adjustment means, there is no need for an expensive cryogenic valve, and this also simplifies the cryogenic piping inside the cold storage tank.
This has the effect of reducing the cost of cryogenic refrigerators.

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

第1図は、従来のヘリウム冷凍機の構成を示す
ブロツク図、第2図は、本発明によるヘリルム冷
凍機の構成の一実施例を示すブロツク図、第3図
は、第2図の固定絞り手段の拡大縦断面図、第4
図は、高圧ラインに導入される高圧GHeの圧力
と冷凍能力との関係線図である。 11……保冷槽、12aないし12e……熱交
換器、13a,13b……膨張機、14……高圧
ライン、15……低圧ライン、43a……圧力調
整弁、60……固定絞り手段。
FIG. 1 is a block diagram showing the configuration of a conventional helium refrigerator, FIG. 2 is a block diagram showing an example of the configuration of a helium refrigerator according to the present invention, and FIG. 3 is a block diagram showing the configuration of a helium refrigerator according to the present invention. Enlarged longitudinal sectional view of the means, 4th
The figure is a diagram showing the relationship between the pressure of high-pressure GHe introduced into the high-pressure line and the refrigerating capacity. 11... Cold storage tank, 12a to 12e... Heat exchanger, 13a, 13b... Expander, 14... High pressure line, 15... Low pressure line, 43a... Pressure regulating valve, 60... Fixed throttle means.

Claims (1)

【特許請求の範囲】[Claims] 1 真空排気される保冷槽内に複数個の熱交換器
を配設し、前記保冷槽内で前記熱交換器の高圧流
路と連通する高圧ラインより分岐し前記熱交換器
の低圧流路と連通する低圧ラインに合流した膨張
機ラインに膨張機を設け、前記高圧ラインの冷媒
出口端に固定絞り手段を設け、前記高圧ラインの
冷媒入口端側で、かつ、前記保冷槽外に冷媒圧力
調整手段を設けたことを特徴とする極低温冷凍
機。
1 A plurality of heat exchangers are arranged in a cold storage tank that is evacuated, and a high pressure line that is connected to a high pressure flow path of the heat exchanger branches within the cold storage tank and connects to a low pressure flow path of the heat exchanger. An expander is provided in an expander line that merges with the communicating low-pressure line, a fixed throttle means is provided at the refrigerant outlet end of the high-pressure line, and a refrigerant pressure adjustment device is provided at the refrigerant inlet end of the high-pressure line and outside the cold storage tank. A cryogenic refrigerator characterized by being provided with means.
JP5831684A 1984-03-28 1984-03-28 Cryogenic refrigerator Granted JPS60205158A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5831684A JPS60205158A (en) 1984-03-28 1984-03-28 Cryogenic refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5831684A JPS60205158A (en) 1984-03-28 1984-03-28 Cryogenic refrigerator

Publications (2)

Publication Number Publication Date
JPS60205158A JPS60205158A (en) 1985-10-16
JPH0349024B2 true JPH0349024B2 (en) 1991-07-26

Family

ID=13080854

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5831684A Granted JPS60205158A (en) 1984-03-28 1984-03-28 Cryogenic refrigerator

Country Status (1)

Country Link
JP (1) JPS60205158A (en)

Also Published As

Publication number Publication date
JPS60205158A (en) 1985-10-16

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