JPH0345862A - cryogenic cooling equipment - Google Patents

cryogenic cooling equipment

Info

Publication number
JPH0345862A
JPH0345862A JP17814689A JP17814689A JPH0345862A JP H0345862 A JPH0345862 A JP H0345862A JP 17814689 A JP17814689 A JP 17814689A JP 17814689 A JP17814689 A JP 17814689A JP H0345862 A JPH0345862 A JP H0345862A
Authority
JP
Japan
Prior art keywords
refrigerant
cooling
gas
cryogenic
nitrogen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP17814689A
Other languages
Japanese (ja)
Inventor
Shigeto Kawamura
河村 成人
Kozo Matsumoto
松本 孝三
Hirotake Kajiwara
梶原 博毅
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 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 Ltd filed Critical Hitachi Ltd
Priority to JP17814689A priority Critical patent/JPH0345862A/en
Publication of JPH0345862A publication Critical patent/JPH0345862A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To utilize efficiently an auxiliary cold source for precooling of a freezing device without uselessly discharging the auxiliary cold source by a method wherein a part of a refrigerant for precooling is branched to the heat shield side of a body to be cooled, and a refrigerant for precooling after cooling of the heat shield is joined with a refrigerant for precooling refrigerant gas. CONSTITUTION:A body 7 to be cooled is placed in a vacuum heat insulating container 8. In order to relieve a heat load on liquid helium, a heat insulating shield plate 9 of a liquid nitrogen temperature level (approximate 80K) is arranged in the vacuum heat insulating layer of the vacuum heat insulating container 8, and the feed of liquid nitrogen to the heat insulating shield plate 9 is effected through liquid nitrogen pipings 10 and 12. In order to maintain the temperature of the heat insulating shield plate 9 at a low value, the temperature of the outlet of a nitrogen piping 13 is kept at an enough low value, and low temperature nitrogen gas is accompanied by a liquid nitrogen mist. The low temperature nitrogen gas accompanied by the liquid nitrogen mist flows through a nitrogen piping 13 and is joined with a liquid nitrogen feed piping 11 to the cold box side. The low temperature nitrogen gas is fed to a cold box 2, and heat-exchanges with helium gas at a heat exchanger 3, the temperature of the nitrogen gas is increased approximately to an ordinary value at a nitrogen outlet piping 14 and released to the open air.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は極低温冷却装置に係り、特に補助寒冷源を用い
るもの)こ好適な極低温冷却装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a cryogenic cooling device, and more particularly to a suitable cryogenic cooling device (using an auxiliary cold source).

〔従来の技術〕[Conventional technology]

従来の装置の一例を第4図により説明する。 An example of a conventional device will be explained with reference to FIG.

′!J4図において、圧縮機1で圧縮されたヘリウムガ
スは、コールドボックス2に入り熱交換器3で、戻りヘ
リウムガスおよび予冷用液体窒素と熱交換を行なったの
ち、一部は、膨張タービン4で、断熱11*u、寒冷を
発生し、低圧ヘリウムガスとなり、圧縮機lの吸入側に
戻る。他の一部のガスは、さらに、熱交換器3で、熱交
換し、温度が下がった状態で、JT弁(ジュール・トム
ソン、mgk弁)5で膨張し、一部が液fヒした状態で
、断熱真空配管6を耗で、超電導マグネット等の被冷却
体7へ送られる。被冷却体を冷却し、蒸発した低温ヘリ
ウムは、断熱真空配管6を経て、コールドボックス2に
戻り、さらに、圧縮機1の吸入側に至る。
′! In Figure J4, the helium gas compressed by the compressor 1 enters the cold box 2 and exchanges heat with the return helium gas and pre-cooling liquid nitrogen in the heat exchanger 3, and then part of it is transferred to the expansion turbine 4. , insulation 11*u, generates cold, becomes low-pressure helium gas, and returns to the suction side of the compressor l. Some of the other gases further undergo heat exchange in the heat exchanger 3, and after the temperature drops, they are expanded in the JT valve (Joule-Thomson, MGK valve) 5, and a part of the gas becomes liquid. Then, the heat insulated vacuum pipe 6 is worn out and the heat is sent to the object 7 to be cooled, such as a superconducting magnet. The low-temperature helium that cools the object to be cooled and evaporates returns to the cold box 2 through the insulated vacuum piping 6, and further reaches the suction side of the compressor 1.

一方、被冷却体7は、真空断熱容器8の内部におかれ、
液体ヘリウムへの熱負荷を軽減するために、真空断熱容
器8の真空断熱層内に、液体窒素温度レベル(約80K
)の断熱シールド板9が設置されている。断熱シールド
板への液体窒素の供給は、液体窒素配管10.およびセ
を経て行なわれる。断熱シールド板9の温度を低温に保
持するためには、窒素配管出口13も十分に低温に保つ
ことになり、−数的に液体窒素ミストを同伴して、大気
へ放出することになる。また、ヘリウム冷凍機の予冷寒
冷として利用される液体窒素は、液体窒素配管10.お
よび11を軽て、コールドボックス2に供給され、熱交
換器3において、ヘリウムガスと熱交換し、窒素出口配
管14では、はぼ常温となって、大気へ放出される。
On the other hand, the object to be cooled 7 is placed inside the vacuum insulation container 8,
In order to reduce the heat load on the liquid helium, the liquid nitrogen temperature level (approximately 80K) is maintained within the vacuum insulation layer of the vacuum insulation container 8.
) is installed. Liquid nitrogen is supplied to the heat insulating shield plate through liquid nitrogen piping 10. This is done through the following steps. In order to maintain the temperature of the heat insulating shield plate 9 at a low temperature, the nitrogen pipe outlet 13 must also be maintained at a sufficiently low temperature, and numerically the liquid nitrogen mist is entrained and released into the atmosphere. In addition, the liquid nitrogen used for pre-cooling of the helium refrigerator is the liquid nitrogen pipe 10. and 11 are then supplied to the cold box 2, where they exchange heat with helium gas in the heat exchanger 3, and at the nitrogen outlet pipe 14, the temperature reaches almost normal temperature and is released into the atmosphere.

なお、この種のシステムとして関連するものには、平成
元年度春期低温工学発表会予備集 B1−3 大内他著
「トリスタン用超伝導四極電磁石の冷却システム(2)
 J P 25 (1989)等が挙げられる。
Related systems of this type include "Cooling System for Superconducting Quadrupole Electromagnet for Tristan (2)" by Ouchi et al., Preliminary Collection of the 1989 Spring Cryogenic Engineering Presentation Conference, B1-3.
J.P. 25 (1989), etc.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記従来技術は補助寒冷源である液体窒素の有効利用に
ついて配慮されておらず、断熱シールド板を冷却した後
の液体窒素がそのまま排出されており、液体窒素の寒冷
が十分に利用されておらず、システムの原単価が悪くな
るという無駄があった。
The above conventional technology does not take into consideration the effective use of liquid nitrogen, which is an auxiliary cooling source, and the liquid nitrogen is discharged as it is after cooling the insulation shield plate, and the cooling power of liquid nitrogen is not fully utilized. , there was a waste in that the unit price of the system deteriorated.

本発明の第1の目的は補助寒冷源を有効に利用すること
のできる極低温冷却装置を提供することにある。
A first object of the present invention is to provide a cryogenic cooling device that can effectively utilize an auxiliary cold source.

本発明の第2の目的は、冷凍機と被冷却体とのそれぞれ
の運転に合わせて効果的に冷却することのできる極低温
冷却装置を提供することにある。
A second object of the present invention is to provide a cryogenic cooling device that can effectively cool a refrigerator and an object to be cooled in accordance with their respective operations.

本発明の第3の目的は、安定した運転を行なうことので
きる極低温冷却装置を提供することにある。
A third object of the present invention is to provide a cryogenic cooling device that can operate stably.

〔課題を解決するための手段〕[Means to solve the problem]

上記第1の目的を達成するために、冷媒ガスを断熱膨張
させて極低温冷奴を生成し、該極低温冷媒により被冷却
体を冷却する極低温冷却装置において、前記冷媒ガスを
予冷する予冷用冷媒の一部を前記被冷却体の熱シールド
側に分岐させ、該熱シールド冷却後の予冷用冷媒を前記
冷媒ガスの予冷用冷媒に合流させたものである。
In order to achieve the above first objective, in a cryogenic cooling apparatus that adiabatically expands a refrigerant gas to generate a cryogenic cold substance and cools an object to be cooled with the cryogenic refrigerant, a pre-cooling device for pre-cooling the refrigerant gas is provided. A part of the refrigerant is branched to the heat shield side of the object to be cooled, and the pre-cooling refrigerant after cooling the heat shield is merged with the pre-cooling refrigerant of the refrigerant gas.

上tel!2の目的を達成するために、冷媒ガスを断熱
膨張させて極低温冷媒を生成する冷凍!kllと。
Upper tel! Refrigeration involves adiabatic expansion of refrigerant gas to produce cryogenic refrigerant in order to achieve the second objective! With kll.

前記生成された極低温冷媒を有する被冷却部と、該被冷
却部に設けられ前記極低温冷媒への熱侵入を防ぐ熱シー
ルド体と、前記冷凍!&置の前記冷媒ガスを予冷する予
冷用冷媒の冷媒供給源と、該冷媒供給源からの予冷用冷
媒の一部を分岐して前記熱シールド体部へ供給する手段
と、前記熱シールド体部からの予冷用冷媒を前記令?1
に装置の予冷部に供給する手段と、前記熱シールド体部
からの予冷用冷奴を排出させる手段と、前記熱シールド
体部からの予冷用冷媒の前記供給と前記排出とを切り換
える手段とから構成したものである。
A cooled part having the generated cryogenic refrigerant, a heat shield provided in the cooled part to prevent heat from entering the cryogenic coolant, and the freezing! a refrigerant supply source of a pre-cooling refrigerant for pre-cooling the refrigerant gas located at &, a means for branching a part of the pre-cooling refrigerant from the refrigerant supply source to the heat shield body, and a means for supplying the pre-cooling refrigerant from the refrigerant supply source to the heat shield body; Is the pre-cooling refrigerant from the above order? 1
a means for supplying the precooling refrigerant to the precooling section of the apparatus; a means for discharging the precooling refrigerant from the heat shield body; and a means for switching between the supply and discharge of the precooling refrigerant from the heat shield body. This is what I did.

上記gJ3の目的を連成するために、冷媒ガスを生皮す
る冷凍装置と、前記生成された極低温冷媒を有する被冷
却部と、該被冷却部に設けられ前記極低温冷媒への熱侵
入を防ぐ熱シールド体と、前記冷凍装置の前記冷媒ガス
を予冷する予冷用冷媒の冷媒供給源と、該冷媒供給源か
らの予冷用冷媒の一部を分岐して前記熱シールド体部へ
供給する手段と、前記熱シールド体部からの予冷用冷媒
を前記冷凍装置の予冷部に供給する手段と、該供給され
る予冷冷媒と前記冷媒供給源から直接に供給される予冷
用冷媒とを気液分離して供給する手段とから構成したも
のである。
In order to couple the purpose of gJ3 above, there is provided a refrigeration device for raw refrigerant gas, a cooled part having the generated cryogenic refrigerant, and a cooling part provided in the cooled part to prevent heat from entering the cryogenic refrigerant. a refrigerant supply source for a precooling refrigerant that precools the refrigerant gas of the refrigeration device, and a means for branching a part of the precooling refrigerant from the refrigerant supply source to the heat shield body. a means for supplying a pre-cooling refrigerant from the heat shield body portion to a pre-cooling section of the refrigeration apparatus; and a means for separating the supplied pre-cooling refrigerant from the pre-cooling refrigerant directly supplied from the refrigerant supply source into a gas-liquid state. and supplying means.

〔作  用〕[For production]

被冷却体の熱シールドから出た予冷用冷媒は、そのまま
大気へ放出すれば、寒冷を失うことになるが、冷凍装置
の予冷寒冷として利用することにより、はぼ常温まで1
1ilF!を回復させることができるので、寒冷の有効
利用が図れる。
If the pre-cooling refrigerant discharged from the heat shield of the object to be cooled is released directly into the atmosphere, it will lose its coldness, but by using it as a pre-cooling cold in the refrigeration equipment, it can be cooled down to almost room temperature by 1.
1ilF! can be recovered, making effective use of cold weather.

また、熱シールドが、比較的高温の予冷時にある場合に
は、熱シールド出口温度が高く、そのまま冷凍装置に供
給すると冷凍装置の温度バランスをくずす恐れがあるが
、熱シールド出口に切換え手段を設けることにより、温
度の高い予冷用冷媒を冷凍装置に供給することなく、大
気へすてることができるので、冷凍装置の制御性が良く
なる。
In addition, when the heat shield is precooling at a relatively high temperature, the heat shield outlet temperature is high, and if it is supplied to the refrigeration equipment as it is, there is a risk of destroying the temperature balance of the refrigeration equipment, but a switching means is provided at the heat shield exit. As a result, the high-temperature precooling refrigerant can be disposed of into the atmosphere without being supplied to the refrigeration system, thereby improving the controllability of the refrigeration system.

さらに、冷凍装置に今冷用冷媒の気液分離を設けること
により、熱シールド板冷却後の予冷用冷媒の影響を受け
ずに、冷凍装置の予冷が安定して行なえる。
Furthermore, by providing the refrigeration system with gas-liquid separation for the current cooling refrigerant, the refrigeration system can be stably precooled without being affected by the precooling refrigerant after cooling the heat shield plate.

〔実 施 例〕〔Example〕

以下、本発明の一実施例を第1図により説明する。 An embodiment of the present invention will be described below with reference to FIG.

!J1図において、lは冷媒ガス、例えば、ヘリウムガ
スを昇圧・循環させる圧縮機、2は真空断熱されたコー
ルドボックス、3は多段に設けられた熱交換器(図示省
略のため取付範囲で図示)、4は寒冷発生用の膨張ター
ビン、5は極低温冷媒発生用のJT弁、6はコールドボ
ックスと真空断熱容器8とをつなぐ断熱真空配管、7は
真空断熱容器8内に収納された被冷却体、9は被冷却体
7への熱侵入を防止する断熱シールド板、10は予冷冷
媒、例えば、液体窒素供給用の配管、■は弁巧を介して
配管10につながり熱交換器3につながる配管、Uは配
管10から断熱シールド板9につながる配管、13は断
熱シールド板9から配管11につながる配管、16は配
管Uに設けた弁である。
! In diagram J1, l is a compressor that boosts and circulates refrigerant gas, such as helium gas, 2 is a vacuum-insulated cold box, and 3 is a multi-stage heat exchanger (the installation range is shown because it is omitted). , 4 is an expansion turbine for cold generation, 5 is a JT valve for generating cryogenic refrigerant, 6 is an insulated vacuum pipe connecting the cold box and the vacuum insulated container 8, and 7 is a cooled object housed in the vacuum insulated container 8. 9 is a heat insulating shield plate that prevents heat from entering the object to be cooled 7; 10 is a pipe for supplying a pre-cooled refrigerant, for example, liquid nitrogen; 2 is connected to the pipe 10 via a valve and connected to the heat exchanger 3; 13 is a pipe connected from the heat insulating shield plate 9 to the pipe 11, and 16 is a valve provided in the pipe U.

上記の構成により、圧縮機lで圧縮されたヘリウムガス
は、コールドボックス2に入り、熱交換器3で、戻りヘ
リウムガスおよび予冷用液体Msと熱交換を行なったの
ち、一部は、膨張タービン4で断熱膨張し、寒冷を発生
し、低圧ヘリウムガスとなり、圧縮1alの吸入側に戻
る。他の一部のガスは、さらに、熱交換器3で熱交換し
、温度が下がった状態でJT弁(ジュール・トムソン膨
張弁)5で膨張し、一部が液化した状態で断熱真空配管
6を経て、超電導マグネット等の被冷却体7へ送られる
。被冷却体7を冷却し、蒸発した低温ヘリウムは、断熱
真空配管6を経て、コールドボックス2に戻り、さらに
、圧縮illの吸入側に至る。
With the above configuration, the helium gas compressed by the compressor 1 enters the cold box 2, and after exchanging heat with the return helium gas and the pre-cooling liquid Ms in the heat exchanger 3, a part of the helium gas is transferred to the expansion turbine. 4, it expands adiabatically, generates cold, becomes low-pressure helium gas, and returns to the suction side of compression 1al. Some of the other gases are further heat-exchanged in a heat exchanger 3, and when the temperature has decreased, they are expanded in a JT valve (Joule-Thomson expansion valve) 5, and a part of the gas is liquefied, which is then heated in an insulated vacuum pipe 6. It is then sent to a cooled object 7 such as a superconducting magnet. The low-temperature helium that cools the object 7 and evaporates returns to the cold box 2 through the adiabatic vacuum piping 6, and further reaches the suction side of the compression ill.

一方、被冷却体7は、真空断熱容器8の内部におかれ、
液体ヘリウムへの熱負荷を軽減するために、真空断熱容
器8の真空断熱層内に、液体窒素温度レベル(約80K
)の断熱シールド板9が設置されている。断熱シールド
板9への液体窒素の供給は、液体窒素配管10.および
セを経て行なわれる。断熱シールド板9の温度を低温に
保持するためには、窒素配管13出口も十分に低温に保
つことになり、液体窒素ミストを同伴する。
On the other hand, the object to be cooled 7 is placed inside the vacuum insulation container 8,
In order to reduce the heat load on the liquid helium, the liquid nitrogen temperature level (approximately 80K) is maintained within the vacuum insulation layer of the vacuum insulation container 8.
) is installed. Liquid nitrogen is supplied to the heat insulating shield plate 9 through liquid nitrogen piping 10. This is done through the following steps. In order to maintain the temperature of the heat insulating shield plate 9 at a low temperature, the outlet of the nitrogen pipe 13 must also be maintained at a sufficiently low temperature, thereby entraining the liquid nitrogen mist.

液体窒素ミストを同伴した、低温窒素ガスは、窒素配管
13を経て、コールドボックス側への液体窒素供給配管
11に合流し、コールドボックス2に供給され、熱交換
器3において、ヘリウムガスと熱交換し、窒素出口配管
14では、はぼ常温となって、大気へ放出される。
The low-temperature nitrogen gas accompanied by the liquid nitrogen mist passes through the nitrogen pipe 13, joins the liquid nitrogen supply pipe 11 to the cold box side, is supplied to the cold box 2, and is heat exchanged with helium gas in the heat exchanger 3. However, in the nitrogen outlet pipe 14, the temperature reaches almost room temperature and is released into the atmosphere.

本実施例によれば、断熱シールド板9の冷却後の液体窒
素および低温窒素ガスの寒冷を顕熱も含めて、ヘリウム
冷凍機の予冷に有効利用できるので、全体として、液体
窒素の消費量を減少できるという経済的効果がある。
According to this embodiment, the cooling of the liquid nitrogen and low-temperature nitrogen gas after cooling the heat insulating shield plate 9, including sensible heat, can be effectively used for pre-cooling the helium refrigerator, so overall the consumption of liquid nitrogen can be reduced. It has the economic effect of reducing

IJ2随に、本発明の第2の実施例を示す。A second embodiment of the present invention will be described below.

182図において、第1図と同符号は同一部材を示し、
説明を消略する。本図が第1図と異なる点は、窒素配管
13の途中に三方弁17を設け、一方は大気放出側とし
た点である。
In Figure 182, the same symbols as in Figure 1 indicate the same members,
Omit the explanation. The difference between this figure and FIG. 1 is that a three-way valve 17 is provided in the middle of the nitrogen pipe 13, and one side is on the atmosphere discharge side.

上記の構成により、断熱シールド板9より出たN素は、
温度が高い予冷時においては、三方弁17において、大
気側に放出し、コールドボックス2側は送らない。断熱
シールド板9より出た窒素の温度が下ってくれば、三方
弁17をコールドボックス2側に切替え、コールドボッ
クス2の予冷に利用する。
With the above configuration, the N element coming out from the heat insulating shield plate 9 is
During precooling when the temperature is high, the three-way valve 17 releases the air to the atmosphere and does not send it to the cold box 2 side. When the temperature of the nitrogen discharged from the heat insulating shield plate 9 falls, the three-way valve 17 is switched to the cold box 2 side and used for pre-cooling the cold box 2.

本実施例によれば、前記一実施例と同様の効果があると
ともに、コールドボックス2側の温度と被冷却体7側の
温度とを独立に管理、運転ができるので、運転制御性が
良くなるという効果がある。
According to this embodiment, the same effects as in the previous embodiment can be obtained, and the temperature on the cold box 2 side and the temperature on the cooled object 7 side can be managed and operated independently, so that operational controllability is improved. There is an effect.

また、窒素温度による三方弁の開閉を自動化すること、
三方弁を二方向弁2台とし、それぞれ、大気側とコール
ドボックス側へ流せるようにし、その流量を制御できる
ようにすることも、同様に有効である。
In addition, automating the opening and closing of the three-way valve depending on the nitrogen temperature,
It is equally effective to replace the three-way valve with two two-way valves so that the flow can flow to the atmosphere side and to the cold box side, respectively, so that the flow rate can be controlled.

第3図に、本発明の第3の実施例を示す。FIG. 3 shows a third embodiment of the invention.

第3図において、第1図および第2図と同符号は同一部
材を示し、説明を省略する。本図においで第2図と異な
る点は、窒素配管11の熱交換器3に入る前に気液分離
1ii18を設け、気体側を熱交換器3の高温側に、液
体側を熱交換器3の低温側に通して予冷可能をこした点
、およびコールドボックス2の液体窒素予冷において、
液体窒素とガス窒素とを分離する気液分離器18の液位
な制御(図示省略)して、適正な液体窒素の供給を可能
とした点である。
In FIG. 3, the same reference numerals as in FIGS. 1 and 2 indicate the same members, and their explanations will be omitted. The difference between this figure and FIG. 2 is that a gas-liquid separation 1ii18 is provided before the nitrogen pipe 11 enters the heat exchanger 3, and the gas side is connected to the high temperature side of the heat exchanger 3, and the liquid side is connected to the heat exchanger 3. In addition, in the liquid nitrogen precooling of the cold box 2,
The point is that the liquid level of the gas-liquid separator 18 that separates liquid nitrogen and gaseous nitrogen is controlled (not shown) to supply an appropriate amount of liquid nitrogen.

断熱シールド板9部の窒素配管13から出てくる液体窒
素ミストの量は、被冷却体7の運転状況によって変わる
が、温度の測定では、直接、把握することができず、ヘ
リウムコールドボックスの温度分布で遅れて検知される
ことになるが、気液分離R18を設けて液面制御するこ
とにより、コールドボックスの液体窒素予冷を安定して
実施でき、運転制御が容易になる。
The amount of liquid nitrogen mist coming out of the nitrogen pipe 13 of the heat insulating shield plate 9 varies depending on the operating status of the object to be cooled 7, but it cannot be directly determined by temperature measurement, and the temperature of the helium cold box varies. Although the detection will be delayed due to the distribution, by providing the gas-liquid separation R18 and controlling the liquid level, the liquid nitrogen precooling of the cold box can be performed stably and operation control becomes easier.

また、気液分離器18の気体部分と流体部分でそれぞれ
に熱交換器3を有効に予冷することができ、さらに予冷
効率を向上できるとともに、予冷用冷媒である液体窒素
の効率的利用が可能となる。
In addition, the heat exchanger 3 can be effectively precooled in the gas and fluid parts of the gas-liquid separator 18, thereby further improving the precooling efficiency and making it possible to efficiently use liquid nitrogen, which is a refrigerant for precooling. becomes.

以上、本実施例によれば、前l!e第2の実施例の効果
に合わせ、上記の効果を得ることができる。
As described above, according to this embodiment, the previous l! eThe above effects can be obtained in accordance with the effects of the second embodiment.

また、本図においては、配管13に温度検出器19を設
け、制御装!加に検出信号を入力して、制御装置加によ
って三方弁17を自動制御可能にしであるが、制御装[
20に冷凍装置側の情報、例えば、停止等を与え、配管
ll側へ流れないように三方弁17を切り換え制御する
ようにすることも可能である。
In addition, in this figure, a temperature detector 19 is provided in the piping 13, and a control device is installed! In addition, a detection signal is inputted to enable automatic control of the three-way valve 17 by the control device.
It is also possible to provide information on the refrigeration system side to 20, such as stop, etc., and to switch and control the three-way valve 17 so as not to flow to the piping 11 side.

なお、これら実施例において、予冷用液体窒素の利用に
被冷却体の断熱シールド板について述べたが、断熱真空
配管6の寒冷移送用の配管等の熱シールドに適用しても
同様の効果が期待できることは云うまでもない。
In addition, in these examples, the heat shield plate of the object to be cooled was described for the use of liquid nitrogen for pre-cooling, but the same effect is expected when applied to the heat shield of the cold transfer pipe of the insulated vacuum pipe 6, etc. It goes without saying that it can be done.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、補助寒冷源を無駄に排出せず冷凍装置
の予冷に有効利用でき、また、全体として補助寒冷源の
消費量を減少できるという経済的効果がある。
According to the present invention, the auxiliary cold source can be effectively used for precooling the refrigeration device without being wastefully discharged, and there is an economical effect that the consumption amount of the auxiliary cold source can be reduced as a whole.

また、切換え手段を設けることに、被冷却体とコールド
ボックスの温度を独立に管理、運転ができるので運転制
御性が良くなるという効果がある。
Furthermore, the provision of the switching means has the effect of improving operational controllability since the temperatures of the object to be cooled and the cold box can be managed and operated independently.

さらに、気液分離器をコールドボックス内に設置するこ
とにより、コールドボックスの予冷を安定して実施でき
るという運転制御上の効果がある。
Furthermore, by installing the gas-liquid separator in the cold box, there is an effect in terms of operation control that precooling of the cold box can be carried out stably.

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

第1図は本発明の一実施例である極低温冷却装置を示す
フロー図、第2図は本発明の第2の一実施例である極低
温冷却装置を示すフロー図、第3図は本発明の第3の一
実施例である極低温冷却装置を示すフロー図、第4図は
従来例の装置を示すフロー図である。 1・・・・・・圧縮機、2・・・・・−コールドボック
ス、3・・・熱交換器、7・・・・・・被冷却体、8・
・−・・真空断熱容器、9・・・・・・断熱シールド板
、10.11.12.13・・−・・配管、ソ 1 図 15、に−−−−−−r 7掖々(P体
FIG. 1 is a flow diagram showing a cryogenic cooling device which is an embodiment of the present invention, FIG. 2 is a flow diagram showing a cryogenic cooling device which is a second embodiment of the present invention, and FIG. FIG. 4 is a flowchart showing a cryogenic cooling device according to a third embodiment of the invention, and FIG. 4 is a flowchart showing a conventional device. 1...Compressor, 2...-cold box, 3...Heat exchanger, 7...Object to be cooled, 8...
...Vacuum insulation container, 9...Insulation shield plate, 10.11.12.13...Piping, 1 Fig. 15, 7... P-body

Claims (1)

【特許請求の範囲】 1、冷媒ガスを断熱膨張させて極低温冷媒を生成し、該
極低温冷媒により被冷却体を冷却する極低温冷却装置に
おいて、前記冷媒ガスを予冷する予冷用冷媒の一部を前
記被冷却体の熱シールド側に分岐させ、該熱シールド冷
却後の予冷用冷媒を前記冷媒ガスの予冷用冷媒に合流さ
せたことを特徴とする極低温冷却装置。 2、前記熱シールド冷却後の予冷用冷媒を排出側へ分岐
させる手段を設けた特許請求の範囲第1項記載の極低温
冷却装置。 3、前記予冷用冷媒の前記冷媒ガス側に気液分離器を設
けた特許請求の範囲第1項記載の極低温冷却装置。 4、冷媒ガスを断熱膨張させて極低温冷媒を生成する冷
凍装置と、前記生成された極低温冷媒を有する被冷却部
と、該被冷却部に設けられ前記極低温冷媒への熱浸入を
防ぐ熱シールド体と、前記冷凍装置の前記冷媒ガスを予
冷する予冷用冷媒の冷媒供給源と、該冷媒供給源からの
予冷用冷媒の一部を分岐して前記熱シールド体部へ供給
する手段と、前記熱シールド体部からの予冷用冷媒を前
記冷凍装置の予冷部に供給する手段と、前記熱シールド
体部からの予冷用冷媒を排出させる手段と、前記熱シー
ルド体部からの予冷用冷媒の前記供給と前記排出とを切
り換える手段とから成ることを特徴とする極低温冷却装
置。 5、冷媒ガスを断熱膨張させて極低温冷媒を生成する冷
凍装置と、前記生成された極低温冷媒を有する被冷却部
と、該被冷却部に設けられ前記極低温冷媒への熱侵入を
防ぐ熱シールド体と、前記冷凍装置の前記冷媒ガスを予
冷する予冷用冷媒の冷媒供給源と、該冷媒供給源からの
予冷用冷媒の一部を分岐して前記熱シールド体部へ供給
する手段と、前記熱シールド体部からの予冷用冷板を前
記冷凍装置の予冷部に供給する手段と、該供給される予
冷用冷媒と前記冷媒供給源から直接に供給される予冷冷
媒とを気液分離して供給する手段とから成ることを特徴
とする極低温冷却装置。
[Claims] 1. In a cryogenic cooling device that adiabatically expands a refrigerant gas to generate a cryogenic refrigerant and cools an object to be cooled with the cryogenic refrigerant, one of the pre-cooling refrigerants that pre-cools the refrigerant gas. A cryogenic cooling device characterized in that a portion is branched to the heat shield side of the object to be cooled, and the precooling refrigerant after cooling the heat shield is merged with the precooling refrigerant of the refrigerant gas. 2. The cryogenic cooling device according to claim 1, further comprising means for branching the precooling refrigerant after cooling the heat shield to the discharge side. 3. The cryogenic cooling device according to claim 1, further comprising a gas-liquid separator on the refrigerant gas side of the pre-cooling refrigerant. 4. A refrigeration device that adiabatically expands refrigerant gas to generate a cryogenic refrigerant, a cooled part having the generated cryogenic refrigerant, and a cooling device installed in the cooled part to prevent heat from penetrating into the cryogenic refrigerant. a heat shield body, a refrigerant supply source of a pre-cooling refrigerant that pre-cools the refrigerant gas of the refrigeration device, and means for branching a part of the pre-cooling refrigerant from the refrigerant supply source to the heat shield body part; , a means for supplying a pre-cooling refrigerant from the heat shield body to a pre-cooling section of the refrigeration apparatus, a means for discharging the pre-cooling refrigerant from the heat shield body, and a pre-cooling refrigerant from the heat shield body. and means for switching between said supply and said discharge. 5. A refrigeration device that adiabatically expands refrigerant gas to generate a cryogenic refrigerant, a cooled part having the generated cryogenic refrigerant, and a cooling device installed in the cooled part to prevent heat from entering the cryogenic coolant. a heat shield body, a refrigerant supply source of a pre-cooling refrigerant that pre-cools the refrigerant gas of the refrigeration device, and means for branching a part of the pre-cooling refrigerant from the refrigerant supply source to the heat shield body part; , a means for supplying a pre-cooling cold plate from the heat shield body portion to a pre-cooling section of the refrigeration apparatus, and a gas-liquid separation means for separating the supplied pre-cooling refrigerant from the pre-cooling refrigerant directly supplied from the refrigerant supply source. A cryogenic cooling device characterized by comprising: means for supplying
JP17814689A 1989-07-12 1989-07-12 cryogenic cooling equipment Pending JPH0345862A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17814689A JPH0345862A (en) 1989-07-12 1989-07-12 cryogenic cooling equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17814689A JPH0345862A (en) 1989-07-12 1989-07-12 cryogenic cooling equipment

Publications (1)

Publication Number Publication Date
JPH0345862A true JPH0345862A (en) 1991-02-27

Family

ID=16043444

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17814689A Pending JPH0345862A (en) 1989-07-12 1989-07-12 cryogenic cooling equipment

Country Status (1)

Country Link
JP (1) JPH0345862A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100466172B1 (en) * 2000-08-31 2005-01-13 주식회사 포스코 Cryogenic treatment method for roll and apparatus of thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100466172B1 (en) * 2000-08-31 2005-01-13 주식회사 포스코 Cryogenic treatment method for roll and apparatus of thereof

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