JPH0349020B2 - - Google Patents
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- Publication number
- JPH0349020B2 JPH0349020B2 JP59050955A JP5095584A JPH0349020B2 JP H0349020 B2 JPH0349020 B2 JP H0349020B2 JP 59050955 A JP59050955 A JP 59050955A JP 5095584 A JP5095584 A JP 5095584A JP H0349020 B2 JPH0349020 B2 JP H0349020B2
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- JP
- Japan
- Prior art keywords
- heat exchanger
- expander
- gas
- cold
- low
- 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 - Lifetime
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Separation By Low-Temperature Treatments (AREA)
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明はヘリウム冷凍機に係り、特に蓄冷器式
膨張機と熱交換器より構成される蓄冷器式のヘリ
ウム冷凍機に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a helium refrigerator, and more particularly to a regenerator-type helium refrigerator comprising a regenerator-type expander and a heat exchanger.
従来のヘリウム冷凍機、特に4.5Kにおける冷
凍能力が10W以下の小容量のものにおいては蓄冷
器式膨張機と熱交換器を組合わせたものが一般で
あつた。その代表的な構成を第1図、第2図によ
つて説明する。
Conventional helium refrigerators, especially small-capacity ones with a refrigerating capacity of 10W or less at 4.5K, generally combine a regenerator type expander and a heat exchanger. A typical configuration thereof will be explained with reference to FIGS. 1 and 2.
第1図で、1は圧縮機(図示せず)から供給さ
れる高圧ヘリウムガスを膨張させて寒冷を発生さ
せる膨張機、2は高圧ガス供給管、3は膨張後の
ガスを圧縮機にもどすためのガス戻し管、4は第
1段膨張機、5は第2段膨張機、6は第1熱交換
器、7は第2熱交換器、8は第3熱交換器、9は
ジユール・トムソン弁(膨張弁でもよい)、10
は第1コールドステーシヨン、11は第2コール
ドステーシヨン、12はふく射シールド、13は
凝縮熱交換器、14は液体ヘリウム容器、15は
真空保冷槽、16は高圧ガス供給管、17は低圧
ガス戻し管である。このようなヘリウム冷凍機
は、米国特許第4277949号明細書等で開示されて
いる。 In Figure 1, 1 is an expander that expands high-pressure helium gas supplied from a compressor (not shown) to generate cold, 2 is a high-pressure gas supply pipe, and 3 is a gas that returns the expanded gas to the compressor. 4 is the first stage expander, 5 is the second stage expander, 6 is the first heat exchanger, 7 is the second heat exchanger, 8 is the third heat exchanger, 9 is the Joule Thomson valve (can also be an expansion valve), 10
1 is a first cold station, 11 is a second cold station, 12 is a radiation shield, 13 is a condensing heat exchanger, 14 is a liquid helium container, 15 is a vacuum cold storage tank, 16 is a high pressure gas supply pipe, and 17 is a low pressure gas return pipe It is. Such a helium refrigerator is disclosed in US Pat. No. 4,277,949 and the like.
また、第1熱交換器6を例にとつて熱交換器の
構造について説明すると、第2図で、18は高熱
伝導材(例えば銅、アルミニウム等)の多孔伝熱
板と低熱伝導材(例えばプラスチツク等)のスペ
ーサを交互に積重ねて接着した積層体、19,2
0はヘツダー、21は積層体18を収納するベツ
セル、22,23は積層体18とベツセル21の
長手方向収縮量の差を吸収するためのベロー、2
4,25は通気孔、26,27は空間、28は低
圧ガスのバイパス流れを防止するシール材、29
は高圧ガス管、30は低圧ガス管である。このよ
うな熱交換器は、実開昭57−127172号公報に開示
されている。 Further, to explain the structure of the heat exchanger using the first heat exchanger 6 as an example, in FIG. A laminate made by alternately stacking and bonding spacers (plastic, etc.), 19,2
0 is a header, 21 is a vessel for storing the laminate 18, 22 and 23 are bellows for absorbing the difference in longitudinal shrinkage between the laminate 18 and the vessel 21, and 2
4 and 25 are ventilation holes, 26 and 27 are spaces, 28 is a sealing material that prevents bypass flow of low pressure gas, and 29
30 is a high pressure gas pipe, and 30 is a low pressure gas pipe. Such a heat exchanger is disclosed in Japanese Utility Model Application No. 57-127172.
次に、このようなヘリウム冷凍機の動作、作用
について説明すると、膨張機1は高圧ガス供給管
2から高圧ヘリウムガスの供給を受けて断熱膨張
させ、それによつて寒冷を発生させ、第1コール
ドステーシヨン10及び第2コールドステーシヨ
ン11を低温にする。断熱膨張したガスはガス戻
し管3から圧縮機にもどる。 Next, to explain the operation and function of such a helium refrigerator, the expander 1 receives high pressure helium gas from the high pressure gas supply pipe 2 and adiabatically expands it, thereby generating cold. The station 10 and the second cold station 11 are made low temperature. The adiabatically expanded gas returns to the compressor through the gas return pipe 3.
一方、高圧ガス供給管16から供給された高圧
ガスは第1熱交換器6を通つてくる間に対向して
流れる低圧流路のガスと熱交換して温度降下し、
第1コールドステーシヨン10に送られる。ここ
で、第1段膨張機4の寒冷発生によつて冷却さ
れ、温度降下して第2熱交換器7に入る。第2熱
交換器7を通る間にも対向して流れる低圧流路の
ガスと熱交換して温度降下し、第2コールドステ
ーシヨン11に送られる。ここで、第2段膨張機
5の寒冷発生によつてさらに冷却され、温度降下
して第3熱交換器8に入る。第3熱交換器8を通
る過程でも同様に対向して流れる低圧ガスと熱交
換して温度降下し、最終的に10K以下になつてジ
ユール・トムソン弁9に至る。ジユール・トムソ
ン弁9を通過するとき低温・高圧のヘリウムガス
は断熱膨張して低温、低圧となりジユール・トム
ソン効果によつて液化する。 On the other hand, while the high-pressure gas supplied from the high-pressure gas supply pipe 16 passes through the first heat exchanger 6, it exchanges heat with the gas in the low-pressure channel flowing oppositely, and its temperature decreases.
It is sent to the first cold station 10. Here, it is cooled by the cold generated by the first stage expander 4, and the temperature drops and enters the second heat exchanger 7. While passing through the second heat exchanger 7, the gas exchanges heat with the gas in the low-pressure flow path that flows opposite to it, lowers its temperature, and is sent to the second cold station 11. Here, the heat is further cooled by the cold generated by the second stage expander 5, and the temperature drops and enters the third heat exchanger 8. In the process of passing through the third heat exchanger 8, the temperature also decreases by exchanging heat with the low pressure gas flowing oppositely, and finally reaches 10K or less and reaches the Joule-Thompson valve 9. When passing through the Joule-Thompson valve 9, the low-temperature, high-pressure helium gas expands adiabatically to become low-temperature and low-pressure, and is liquefied by the Joule-Thompson effect.
液化したあと、気液混入の流体は凝縮熱交換器
13に入り、ここで、液体ヘリウム容器14の中
の気化ガスと熱交換し、管外で気化ガスを再凝縮
させると同時に自身は管内で気化して第3熱交換
器8、第2熱交換器7、第1熱交換器6の低圧ガ
ス流路を順次通り、対向して流れる高圧ガスを冷
却しながら自身は温度上昇し、最終的には常温に
なつて低圧ガス戻し管17を経て圧縮機にもど
る。 After being liquefied, the gas-liquid mixed fluid enters the condensing heat exchanger 13, where it exchanges heat with the vaporized gas in the liquid helium container 14, recondensing the vaporized gas outside the tube, and at the same time recondensing the vaporized gas inside the tube. It vaporizes and sequentially passes through the low-pressure gas channels of the third heat exchanger 8, second heat exchanger 7, and first heat exchanger 6, and while cooling the high-pressure gas flowing in the opposite direction, its temperature rises, and finally When the temperature reaches room temperature, the gas returns to the compressor via the low-pressure gas return pipe 17.
また真空保冷槽15の内側は定常運転時には
10-6Torr以下の真空圧力に保持され、外部から
低温部へのガス対流による熱侵入を低減する作用
を行なう。ふく射シールド12は同様に常温の真
空保冷槽15の壁面から低温部へのふく射による
熱侵入を低減する作用を行なうもので、第1段膨
張機4の低温端及び第1熱交換器6の低温部、ま
たは第1熱交換器6〜第2熱交換器7の間の配管
等々に接触させることによつて冷却するのが一般
である。 In addition, the inside of the vacuum cold storage tank 15 is
It is maintained at a vacuum pressure of 10 -6 Torr or less, and has the effect of reducing heat intrusion from the outside to the low-temperature part due to gas convection. The radiation shield 12 similarly functions to reduce heat intrusion due to radiation from the wall surface of the vacuum cold storage tank 15 at room temperature to the low-temperature part, and is used to reduce the heat intrusion due to radiation from the wall surface of the room-temperature vacuum cold storage tank 15 to the low-temperature end of the first stage expander 4 and the low-temperature end of the first heat exchanger 6. Generally, cooling is performed by bringing the heat exchanger into contact with the heat exchanger 6 or the piping between the first heat exchanger 6 and the second heat exchanger 7, or the like.
このような従来のヘリウム冷凍機には次のよう
な欠点があつた。すなわち、複数の熱交換器間、
及び熱交換器〜膨張機間を連絡する配管が複雑で
あるために製作費が高くなるうえ、配管の接続個
所が多くなるのでガスリークを発生する機会が増
して信頼性が低下するという欠点があつた。特に
小容量のヘリウム冷凍機においては、このような
欠点は致命的なものとなる。 Such conventional helium refrigerators have the following drawbacks. That is, between multiple heat exchangers,
The piping that connects the heat exchanger and the expander is complicated, which increases production costs, and the increased number of piping connections increases the chance of gas leaks, reducing reliability. Ta. Particularly in small-capacity helium refrigerators, such drawbacks are fatal.
本発明の目的は熱交換器間及び熱交換器〜膨張
機間を連絡する配管をなくし、構造が簡単で信頼
性の高いヘリウム冷凍機を提供することにある。
An object of the present invention is to provide a helium refrigerator that has a simple structure and high reliability by eliminating piping that communicates between heat exchangers and between a heat exchanger and an expander.
本発明は、高圧ヘリウムガスを断熱膨張させる
ことによつて寒冷を発生する膨張機と、膨張機と
は離して設けられ戻りの低圧ヘリウムガスと高圧
ヘリウムガスとの流路が形成された中間ヘツダー
を介して複数個が接続された熱交換器とを有する
ヘリウム冷凍機において、膨張機の寒冷発生部と
熱交換器の中間ヘツダーとを可撓性の熱連絡体を
介して連結することにより、熱交換器間及び熱交
換器と膨張機との間を連絡する配管をなくして、
構造を簡単にするとともに信頼性を高くしたもの
である。
The present invention provides an expander that generates cold by adiabatic expansion of high-pressure helium gas, and an intermediate header that is separated from the expander and has a flow path for return low-pressure helium gas and high-pressure helium gas. In a helium refrigerator having a plurality of heat exchangers connected through Eliminating piping that connects between heat exchangers and between the heat exchanger and the expander,
The structure is simplified and reliability is increased.
以下、本発明の一実施例を第3図により説明す
る。まず、構成について説明すると、31は膨張
機、32は圧縮機(図示せず)から供給される膨
張機31への高圧ガス供給管、33は膨張後の低
圧ガスを圧縮機にもどすためのガス戻し管、34
は第1段膨張機、35は第2段膨張機、36は第
1熱交換器、37は第2熱交換器、38は第3熱
交換器、39はジユール・トムソン弁、40は第
1コールドステーシヨン、41は第2コールドス
テーシヨン、42はふく射シールド、43は凝縮
熱交換器、44は液体ヘリウム槽、45は真空保
冷槽、46は第1熱交換器36への高圧ガス供給
管、47は第1熱交換器36から圧縮器への低圧
ガス戻し管、48は第1熱交換器36の常温側ヘ
ツダー、49,50は熱交換器間に設けた中間ヘ
ツダー、51は第3熱交換器38の低温側ヘツダ
ー、52は第1コールドステーシヨン40と中間
ヘツダー49を結ぶ熱連絡体、53は第2コール
ドステーシヨン41と中間ヘツダー50を結ぶ熱
連絡体である。
An embodiment of the present invention will be described below with reference to FIG. First, to explain the configuration, 31 is an expander, 32 is a high pressure gas supply pipe to the expander 31 supplied from a compressor (not shown), and 33 is a gas for returning low pressure gas after expansion to the compressor. Return pipe, 34
is the first stage expander, 35 is the second stage expander, 36 is the first heat exchanger, 37 is the second heat exchanger, 38 is the third heat exchanger, 39 is the Juul-Thompson valve, 40 is the first Cold station, 41 is a second cold station, 42 is a radiation shield, 43 is a condensing heat exchanger, 44 is a liquid helium tank, 45 is a vacuum cold storage tank, 46 is a high pressure gas supply pipe to the first heat exchanger 36, 47 is a low-pressure gas return pipe from the first heat exchanger 36 to the compressor, 48 is a normal temperature side header of the first heat exchanger 36, 49 and 50 are intermediate headers provided between the heat exchangers, and 51 is a third heat exchanger. 52 is a thermal connector connecting the first cold station 40 and the intermediate header 49; 53 is a thermal connector connecting the second cold station 41 and the intermediate header 50.
次に作用について説明すると、高圧ガス供給管
46に送られた常温、高圧のガスは常温側ヘツダ
ー48を経て第1熱交換器36に送られる。第1
熱交換器36を通過する過程で対向して流れる低
圧ガスで冷却され、温度降下して中間ヘツダー4
9に入る。中間ヘツダー49は熱連絡体52を介
して第1段膨張機34の発生寒冷によつて冷却さ
れているので、高圧ガスは中間ヘツダー49を通
過する際に温度降下して第2熱交換器37に入
る。第2熱交換器37でも同様に対向して流れる
低圧ガスが冷却され、温度降下して中間ヘツダー
50に送られる。中間ヘツダー50は熱連絡体5
3を介して第2段膨張機35の発生寒冷によつて
冷却されているので、ここでも高圧ガスは冷却さ
れて第3熱交換器38に入り、対向して流れる低
圧ガスで冷却され、最終的には10K以下になつて
ジユール・トムソン弁39に至る。ジユール・ト
ムソン弁39を通過するときに低温・高圧のヘリ
ウムガスは断熱膨張して低温・低圧になり、ジユ
ール・トムソン効果によつて液化する。 Next, the operation will be explained. The normal temperature, high pressure gas sent to the high pressure gas supply pipe 46 is sent to the first heat exchanger 36 via the normal temperature side header 48. 1st
In the process of passing through the heat exchanger 36, it is cooled by the low pressure gas flowing oppositely, and the temperature drops and the intermediate header 4
Enter 9. Since the intermediate header 49 is cooled by the cold generated by the first stage expander 34 via the thermal communication body 52, the temperature of the high pressure gas decreases when passing through the intermediate header 49, and the high pressure gas is transferred to the second heat exchanger 37. to go into. Similarly, in the second heat exchanger 37, the low-pressure gas flowing oppositely is cooled and sent to the intermediate header 50 with a reduced temperature. The intermediate header 50 is the thermal connector 5
3, the high-pressure gas is cooled by the cold generated by the second-stage expander 35, so the high-pressure gas is cooled here as well and enters the third heat exchanger 38, where it is cooled by the low-pressure gas flowing oppositely to the final The target becomes less than 10K and reaches Juul-Thomson valve 39. When passing through the Joule-Thompson valve 39, the low-temperature, high-pressure helium gas undergoes adiabatic expansion, becomes low-temperature and low-pressure, and liquefies due to the Joule-Thompson effect.
液化した後、凝縮熱交換器43に入り、ここで
液体ヘリウム容器44の中の気化ガスを再凝縮さ
せると同時に自身は気化して第3熱交換器38、
第2熱交換器37、第1熱交換器36の低圧流路
を通り、対向して流れる高圧ガスを冷却しながら
自身は昇温し、最終的に常温になつて低圧ガス戻
し管47を経て圧縮機にもどる。 After being liquefied, it enters the condensing heat exchanger 43, where it re-condenses the vaporized gas in the liquid helium container 44 and at the same time vaporizes itself into the third heat exchanger 38,
It passes through the low-pressure flow path of the second heat exchanger 37 and the first heat exchanger 36, and while cooling the high-pressure gas flowing oppositely, the temperature of the high-pressure gas itself rises, and finally reaches room temperature and passes through the low-pressure gas return pipe 47. Back to the compressor.
本実施例における特徴は3つの熱交換器を2つ
の中間ヘツダーを介して一体化することにより、
配管を極力少なくしたことであり、さらに別の特
徴は膨張機〜熱交換器管の熱の授受において表面
にアルミ蒸着してふく射伝熱よる熱侵入を防いだ
銅網帯のようなフレキシブルな熱連絡体を用いる
ことにより、膨張機系統と熱交換器系統の間を連
絡するヘリウムガス配管をなくしたことである。 The feature of this embodiment is that three heat exchangers are integrated via two intermediate headers.
Another feature is that the number of piping has been minimized, and another feature is that a flexible heat exchanger, such as a copper mesh band, is used to transfer heat from the expander to the heat exchanger tube, and the surface is vapor-deposited with aluminum to prevent heat intrusion due to radiant heat transfer. By using a connecting body, the helium gas piping that connects the expander system and the heat exchanger system can be eliminated.
本実施例によれば、複数の熱交換器を中間ヘツ
ダーを介して接続し、膨張機の寒冷発生部と熱交
換器の中間ヘツダーとを可撓性の熱連絡体を介し
て連結しているので、熱交換器間及び膨張機と熱
交換器との間を連結するガス配管がなくなるとと
もに、可撓性の熱連絡体によつて膨張機の寒冷発
生部と熱交換器の中間ヘツダーとの間を簡単に連
結できるので構造が簡単になり、また、配管の接
続不良等に起因するガス洩れ等もなくなり信頼性
が向上するという効果がある。 According to this embodiment, a plurality of heat exchangers are connected via intermediate headers, and the cold generation part of the expander and the intermediate header of the heat exchanger are connected via a flexible thermal link. Therefore, there is no need for gas piping to connect between the heat exchangers or between the expander and the heat exchanger, and flexible thermal interconnects are used to connect the cold generation part of the expander and the intermediate header of the heat exchanger. The structures can be easily connected, which simplifies the structure, and also eliminates gas leaks caused by poor piping connections, improving reliability.
第4図は本発明の他の実施例を示すもので第1
熱交換器36の具体的な構造について説明すると
54は外筒部、55は多孔伝熱板とスペーサを交
互に積重ねて接着した積層体、56は外筒部の一
部に接続されたベロー、57,58はガス通気孔
である。 FIG. 4 shows another embodiment of the present invention.
To explain the specific structure of the heat exchanger 36, 54 is an outer cylinder part, 55 is a laminate in which porous heat exchanger plates and spacers are alternately stacked and bonded, 56 is a bellows connected to a part of the outer cylinder part, 57 and 58 are gas vents.
この場合は積層体55と外筒部54の長手方向
収縮量の差を前記ベロー56で吸収する。 In this case, the bellows 56 absorbs the difference in the amount of longitudinal shrinkage between the laminate 55 and the outer cylindrical portion 54 .
本実施例によれば、外筒部54の一部にベロー
56を接続するだけでよいから第2図に示す従来
例に比して構造が簡単になるうえ、低圧ガス配管
も直接ヘツダー48に接合するので低圧ガスのバ
イパス流れを生ずることがないという効果があ
る。 According to this embodiment, since it is only necessary to connect the bellows 56 to a part of the outer cylindrical portion 54, the structure is simpler than that of the conventional example shown in FIG. Since they are joined, there is an effect that bypass flow of low pressure gas does not occur.
第5図は本発明のさらに他の実施例を示すもの
で、第1膨張機34の第1コールドステーシヨン
と第1熱交換器36と第2熱交換器37の中間ヘ
ツダーを結ぶ熱連絡体52及び第2コールドステ
ーシヨンと第2熱交換器37と第3熱交換器38
の中間ヘツダーを結ぶ熱連絡体53をそれぞれコ
ールドステーシヨンや中間ヘツダーの周りに固定
するため止金具61,62,63,64を分割形
にしたことにより、膨張機と熱交換器群を別々に
組立てた後、熱連絡体52,53を単独に取付け
たり、取外すことができるので組立作業が容易に
なるという効果がある。 FIG. 5 shows still another embodiment of the present invention, in which a thermal link 52 connects the first cold station of the first expander 34 and the intermediate headers of the first heat exchanger 36 and second heat exchanger 37. and a second cold station, a second heat exchanger 37, and a third heat exchanger 38
The expansion machine and the heat exchanger group can be assembled separately by dividing the fasteners 61, 62, 63, and 64 in order to fix the thermal connecting body 53 connecting the intermediate headers around the cold station and the intermediate header, respectively. After that, the thermal interconnects 52 and 53 can be attached or removed individually, which has the effect of facilitating assembly work.
本発明によれば、複数の熱交換器を中間ヘツダ
ーを介して接続し、膨張機の寒冷発生部と熱交換
器の中間ヘツダーとを可撓性の熱連絡体で連結す
ることによつて、熱交換器間及び熱交換器と膨張
機との間を連結する配管をなくすことができると
ともに、膨張機の寒冷発生部と熱交換器の中間ヘ
ツダーとの間を簡単に連結できるので、構造を簡
単にできるうえ、配管接続部の減少によつて信頼
性が向上するという効果がある。
According to the present invention, by connecting a plurality of heat exchangers via an intermediate header and connecting the cold generation part of the expander and the intermediate header of the heat exchanger with a flexible thermal connecting body, It is possible to eliminate the piping that connects the heat exchangers and between the heat exchanger and the expander, and it is also possible to easily connect between the cold generation part of the expander and the intermediate header of the heat exchanger, which reduces the structure. Not only is it easy to do, but it also has the effect of improving reliability by reducing the number of piping connections.
第1図は従来の蓄冷器式のヘリウム冷凍機の構
成を示すシステム系統図、第2図は従来のヘリウ
ム冷凍機に適用されている積層熱交換器の断面
図、第3図は本発明による蓄冷器式のヘリウム冷
凍機の構成の一実施例を示すシステム系統図、第
4図は本発明によるヘリウム冷凍機の他の実施例
を示す一体形積層熱交換器の部分断面図、第5図
は本発明によるヘリウム冷凍機の更に他の実施例
を示す膨張機と熱交換器を結ぶ熱連絡体の取付状
態側面図である。
31……膨張機、40……第1コールドステー
シヨン、41……第2コールドステーシヨン、3
6……第1熱交換器、37……第2熱交換器、3
8……第3熱交換器、49,50……中間ヘツダ
ー、52,53……熱連絡体。
Fig. 1 is a system diagram showing the configuration of a conventional regenerator-type helium refrigerator, Fig. 2 is a sectional view of a laminated heat exchanger applied to a conventional helium refrigerator, and Fig. 3 is a system diagram according to the present invention. FIG. 4 is a system system diagram showing one embodiment of the configuration of a regenerator-type helium refrigerator; FIG. 4 is a partial sectional view of an integrated laminated heat exchanger showing another embodiment of the helium refrigerator according to the present invention; FIG. FIG. 2 is a side view showing a state in which a thermal connecting body connecting an expander and a heat exchanger is installed, showing still another embodiment of a helium refrigerator according to the present invention. 31... Expander, 40... First cold station, 41... Second cold station, 3
6...First heat exchanger, 37...Second heat exchanger, 3
8... Third heat exchanger, 49, 50... Intermediate header, 52, 53... Heat communication body.
Claims (1)
つて寒冷を発生する膨張機と、前記膨張機とは離
して設けられ戻りの低圧ヘリウムガスと高圧ヘリ
ウムガスとの流路が形成された中間ヘツダーを介
して複数個が接続された熱交換器と、該熱交換器
によつて冷却された高圧ヘリウムガスを断熱膨張
させて液化に導く膨張弁とを有して成り、前記膨
張機の寒冷発生部と前記熱交換器の中間ヘツダー
とを可撓性の熱連絡体を介して連結したことを特
徴とするヘリウム冷凍機。 2 前記熱連絡体は少なくとも前記膨張機の寒冷
発生部または前記熱交換器の中間ヘツダーのいづ
れかに着脱可能に連結した特許請求の範囲第1項
記載のヘリウム冷凍機。[Scope of Claims] 1. An expander that generates cold by adiabatic expansion of high-pressure helium gas, and a flow path provided separately from the expander for return low-pressure helium gas and high-pressure helium gas. a plurality of heat exchangers connected through intermediate headers, and an expansion valve that adiabatically expands high-pressure helium gas cooled by the heat exchanger and leads it to liquefaction, 1. A helium refrigerator, characterized in that a cold generation part of the refrigerator and an intermediate header of the heat exchanger are connected via a flexible thermal link. 2. The helium refrigerator according to claim 1, wherein the thermal communication body is detachably connected to at least one of the cold generation part of the expander or the intermediate header of the heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5095584A JPS60196564A (en) | 1984-03-19 | 1984-03-19 | Helium refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5095584A JPS60196564A (en) | 1984-03-19 | 1984-03-19 | Helium refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60196564A JPS60196564A (en) | 1985-10-05 |
| JPH0349020B2 true JPH0349020B2 (en) | 1991-07-26 |
Family
ID=12873241
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5095584A Granted JPS60196564A (en) | 1984-03-19 | 1984-03-19 | Helium refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60196564A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60123563U (en) * | 1984-01-30 | 1985-08-20 | 住友重機械工業株式会社 | small helium refrigerator |
-
1984
- 1984-03-19 JP JP5095584A patent/JPS60196564A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60196564A (en) | 1985-10-05 |
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