JPH0541320Y2 - - Google Patents

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Publication number
JPH0541320Y2
JPH0541320Y2 JP1986177329U JP17732986U JPH0541320Y2 JP H0541320 Y2 JPH0541320 Y2 JP H0541320Y2 JP 1986177329 U JP1986177329 U JP 1986177329U JP 17732986 U JP17732986 U JP 17732986U JP H0541320 Y2 JPH0541320 Y2 JP H0541320Y2
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Japan
Prior art keywords
flow path
refrigerant
liquid
gas
throttle
Prior art date
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Expired - Lifetime
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JP1986177329U
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Japanese (ja)
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JPS6382171U (en
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Publication of JPS6382171U publication Critical patent/JPS6382171U/ja
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Description

【考案の詳細な説明】 (産業上の利用分野) この考案は、圧縮機潤滑油を溶解するための比
較的高沸点の冷媒を含む、それぞれ異なつた沸点
を有する複数の冷媒から成る混合冷媒を用いた低
温冷凍機に関する。
[Detailed description of the invention] (Field of industrial application) This invention uses a mixed refrigerant consisting of multiple refrigerants each having a different boiling point, including a refrigerant with a relatively high boiling point for dissolving compressor lubricating oil. Regarding the low-temperature refrigerator used.

(従来の技術とその問題点) 従来この種の低温冷凍機として、例えば実公昭
55−2374号公報の第3図に開示されたものが知ら
れている。この低温冷凍機では、混合冷媒に対
し、混合冷媒中の最高沸点の冷媒よりも高い沸点
を有しかつ、採用される圧縮機潤滑油との高度の
混和性あるいは溶解度を有する分離液が添加され
る。この混合冷媒は高温気相状態において圧縮機
で圧縮され、第1凝縮器段階で部分的に凝縮され
て、気液混合冷媒となる。このとき分離液のほぼ
全量が凝縮され、これを気液分離することにより
分離液に溶解した圧縮機潤滑油を回収して、圧縮
機潤滑油が低温域にまわらないように残りの気相
混合冷媒から分離している。
(Conventional technology and its problems) Conventionally, as this type of low-temperature refrigerator, for example, Jikkosho
The one disclosed in FIG. 3 of Japanese Patent No. 55-2374 is known. In this low-temperature refrigerator, a separated liquid is added to the mixed refrigerant, which has a boiling point higher than the refrigerant with the highest boiling point in the mixed refrigerant and has a high degree of miscibility or solubility with the compressor lubricating oil used. Ru. This mixed refrigerant is compressed in a compressor in a hot gaseous state and partially condensed in a first condenser stage to form a gas-liquid mixed refrigerant. At this time, almost all of the separated liquid is condensed, and by separating it into gas and liquid, the compressor lubricating oil dissolved in the separated liquid is recovered, and the remaining gas phase is mixed to prevent the compressor lubricating oil from reaching the low temperature range. Separated from refrigerant.

しかしながら実際の運転においては、圧縮機潤
滑油の分離は100%ではなく、わずかずつではあ
るが分離されずに低温域の方へと漏洩する。良質
の潤滑油は比較的高い流動点を有するので、漏洩
した潤滑油は低温域では流動しなくなり、これが
蓄積されて、長期の連続運転では配管内、特に径
の細いキヤピラリチユーブなどを閉塞して管詰り
現象を発生するという問題があつた。
However, in actual operation, the separation of the compressor lubricating oil is not 100%, and it leaks into the low temperature region little by little without being separated. Since good quality lubricating oil has a relatively high pour point, leaked lubricating oil will no longer flow at low temperatures, and will accumulate and cause blockage in piping, especially small-diameter capillary tubes, during long-term continuous operation. There was a problem that pipe clogging occurred.

(考案の目的) そこでこの考案の目的は、圧縮機潤滑油を溶解
した混合冷媒を用いる冷凍システムにおいて、長
期連続運転によつても管詰り現象が生ずることの
ない低温冷凍機を提供することである。
(Purpose of the invention) Therefore, the purpose of this invention is to provide a low-temperature refrigerator that does not cause pipe clogging even during long-term continuous operation in a refrigeration system that uses a mixed refrigerant in which compressor lubricating oil is dissolved. be.

(目的を達成するための手段) 上記目的を達成するため、この考案による低温
冷凍機は、圧縮機潤滑油を溶解するための比較的
高沸点の第1の冷媒を含むそれぞれ異なつた沸点
を有する複数の冷媒から成る高温気相状態の混合
冷媒を圧縮するための圧縮機と、前記混合冷媒を
前記圧縮機に導入する帰還流路と、前記圧縮機で
圧縮された混合冷媒を部分的に凝縮させ、少なく
とも前記第1の冷媒を液相の状態として含んだ気
液混合冷媒を作り出す凝縮器と、前記気液混合冷
媒を気相冷媒と液相冷媒とに分離する気液分離器
と、前記帰還流路上に設けられ、前記気液分離器
により分離された気相冷媒を、前記帰還流路を流
れる冷媒との熱交換により少なくとも部分的に凝
縮させて、低温の液相もしくは気液混合冷媒を作
り出す複数の熱交換器と、前記気液分離器により
分離された液相冷媒を減圧膨張させ、この減圧膨
張させた液相冷媒を、前記熱交換器のうち帰還流
路の最上流側に位置する熱交換器を除く所定の熱
交換器の直上流において前記帰還流路に合流させ
る第1の絞り流路と、前記第1の絞り流路との合
流点より前記帰還流路上において下流側に位置す
る熱交換器による部分凝縮により得られた液相冷
媒を減圧膨張させて、前記第1の絞り流路よりも
前記帰還流路上において上流側に位置する熱交換
器の直上流で前記帰還流路に合流させる第2の絞
り流路と、前記第1の絞り流路よりも前記帰還流
路上において上流側に位置する熱交換器により得
られた低温液相冷媒を減圧膨張させる第3の絞り
流路と、前記第3の絞り流路により減圧膨張され
た低温液相冷媒を少なくとも部分的に蒸発させる
ことにより低温冷却し、前記帰還流路の上流端に
導入する冷却器とを備えるとともに、前記気液分
離器により気相冷媒と分離された液相冷媒を、前
記第2の絞り流路または第3の絞り流路のうちの
少なくとも一の絞り流路の直上流に合流させるバ
イパス流路と、このバイパス流路を開閉する開閉
手段とをさらに備えている。この考案による低温
冷凍機は、上記のような構成上の特徴を備えるこ
とにより、低温域において流動しなくなつた圧縮
機潤滑油を比較的高温でかつ圧縮機潤滑油に対し
高い溶解度を有する液相冷媒により洗浄できる。
(Means for Achieving the Object) In order to achieve the above object, the cryogenic refrigerator according to this invention includes a first refrigerant having a relatively high boiling point for dissolving compressor lubricating oil, each having a different boiling point. a compressor for compressing a mixed refrigerant in a high-temperature vapor phase consisting of a plurality of refrigerants; a return passage for introducing the mixed refrigerant into the compressor; and a partial condensation of the mixed refrigerant compressed by the compressor. a condenser that produces a gas-liquid mixed refrigerant containing at least the first refrigerant in a liquid phase; a gas-liquid separator that separates the gas-liquid mixed refrigerant into a gas-phase refrigerant and a liquid-phase refrigerant; The gas phase refrigerant provided on the return flow path and separated by the gas-liquid separator is at least partially condensed by heat exchange with the refrigerant flowing through the return flow path to produce a low-temperature liquid phase or gas-liquid mixed refrigerant. a plurality of heat exchangers that produce a a first throttle flow path that joins the return flow path immediately upstream of a predetermined heat exchanger other than the heat exchanger located therein, and a downstream side on the return flow path from the confluence with the first throttle flow path; The liquid phase refrigerant obtained by partial condensation by the heat exchanger located at a second throttle flow path that joins the flow path; and a third throttle flow path that depressurizes and expands the low-temperature liquid phase refrigerant obtained by a heat exchanger located upstream of the return flow path than the first throttle flow path. a throttle flow path; and a cooler that cools the low-temperature liquid phase refrigerant that has been depressurized and expanded by the third throttle flow path by at least partially evaporating it and introduces it into the upstream end of the return flow path; , a bypass flow in which the liquid phase refrigerant separated from the gas phase refrigerant by the gas-liquid separator joins immediately upstream of at least one of the second throttle channel or the third throttle channel; The bypass flow path is further provided with an opening/closing means for opening and closing the bypass flow path. By having the above-mentioned structural features, the low-temperature refrigerator according to this invention converts the compressor lubricating oil, which has stopped flowing in the low-temperature range, into a relatively high-temperature liquid that has high solubility in the compressor lubricating oil. Can be cleaned with phase refrigerant.

(実施例) 図面はこの発明による低温冷凍機の一実施例を
示す構成図である。この低温冷凍機において、冷
媒には、それぞれ異なつた沸点を有する複数の冷
媒から成る混合冷媒を用いる。さらに混合冷媒中
の比較的高沸点の冷媒として、例えばR11,R
12等の圧縮機潤滑油との溶解性の優れたものを
使用し、この比較的高沸点の冷媒に圧縮機潤滑油
を溶解させて、図示の低温冷凍機に適用する。
(Embodiment) The drawing is a configuration diagram showing an embodiment of a low temperature refrigerator according to the present invention. In this low-temperature refrigerator, a mixed refrigerant consisting of a plurality of refrigerants each having a different boiling point is used as the refrigerant. Furthermore, as a refrigerant with a relatively high boiling point in the mixed refrigerant, for example, R11, R
A refrigerant having excellent solubility with the compressor lubricating oil, such as No. 12, is used, and the compressor lubricating oil is dissolved in this relatively high boiling point refrigerant, and the refrigerant is applied to the illustrated low-temperature refrigerator.

高温気相状態の混合冷媒は圧縮機1で圧縮後、
導管2を通じて凝縮器3に送られ、そこで部分的
に凝縮される。凝縮器3は例えば、送風機4によ
り送られる空気流との熱交換により混合冷媒を部
分的に凝縮させる。さらに凝縮器3の後段に補助
凝縮器を設けて、圧縮機1への帰還流路5を流れ
る冷媒との熱交換により、凝縮器3による凝縮を
促進するようにしてもよい。
After the mixed refrigerant in the high temperature vapor phase is compressed by the compressor 1,
It is passed through conduit 2 to condenser 3 where it is partially condensed. The condenser 3 partially condenses the mixed refrigerant, for example by exchanging heat with an air stream sent by a blower 4. Furthermore, an auxiliary condenser may be provided after the condenser 3 to promote condensation by the condenser 3 through heat exchange with the refrigerant flowing through the return passage 5 to the compressor 1.

このようにして部分的に凝縮された気液混合冷
媒は、導管6を通じて気液分離器7に送られ、気
相冷媒と液相冷媒とに分離される。この分離され
た液相冷媒は比較的高沸点のものであり、この中
には上述したR11,R12等の圧縮機潤滑油を
溶解したものも含まれる。したがつてこの段階で
圧縮機潤滑油は、液相冷媒に解け込んだ状態で気
相冷媒から分離されて回収される。もつとも100
%完全に分離されるわけではなく、気相冷媒中に
若干紛れ込んで、低温域において管詰まり現象の
原因になることは上述したとおりである。
The gas-liquid mixed refrigerant thus partially condensed is sent through the conduit 6 to the gas-liquid separator 7, where it is separated into a gas-phase refrigerant and a liquid-phase refrigerant. This separated liquid-phase refrigerant has a relatively high boiling point, and includes dissolved compressor lubricating oils such as R11 and R12 described above. Therefore, at this stage, the compressor lubricating oil is separated from the gaseous refrigerant and recovered in a state dissolved in the liquid refrigerant. At least 100
As mentioned above, it is not completely separated, but some amount gets mixed into the gas phase refrigerant, causing pipe clogging in the low temperature range.

気液分離器7により分離された液相冷媒は、キ
ヤピラリチユーブから成る絞り流路8により減圧
膨張されて、第1熱交換器9の上流側において、
圧縮機1への帰還流路5に合流される。気液分離
器7により分離された気相冷媒は、導管10を通
じて第1熱交換器9に送られ、そこで帰還流路5
を流れる冷媒との熱交換により部分的に凝縮され
て、気液混合冷媒となる。
The liquid phase refrigerant separated by the gas-liquid separator 7 is depressurized and expanded by the throttle channel 8 consisting of a capillary tube, and is then expanded at the upstream side of the first heat exchanger 9.
It is merged into a return flow path 5 to the compressor 1. The gas phase refrigerant separated by the gas-liquid separator 7 is sent through the conduit 10 to the first heat exchanger 9, where it is passed through the return flow path 5.
It is partially condensed by heat exchange with the refrigerant flowing through the refrigerant, and becomes a gas-liquid mixed refrigerant.

こうして得られた液相冷媒のうちの一部は、キ
ヤピラリチユーブから成る絞り流路11へと導か
れ、そこで減圧膨張されて、第2熱交換器12の
上流側において帰還流路5に合流される。残りの
液相冷媒および気相冷媒は、導管13を通じて第
2熱交換器12へと導かれ、そこで全てまたは部
分的に凝縮して、低温の液相もしくは気液混合冷
媒となる。なお第1熱交換器9により得られた気
液混合冷媒を気液分離器により分離し、液相冷媒
を絞り流路11を介して帰還流路5に合流させ、
気相冷媒を第2熱交換器12に導く構成をとるこ
とも可能である。
A part of the liquid phase refrigerant obtained in this way is guided to the throttle channel 11 consisting of a capillary tube, is depressurized and expanded there, and joins the return channel 5 on the upstream side of the second heat exchanger 12. be done. The remaining liquid and vapor phase refrigerants are conducted through conduit 13 to second heat exchanger 12 where they are wholly or partially condensed into a low temperature liquid phase or gas-liquid mixture refrigerant. Note that the gas-liquid mixed refrigerant obtained by the first heat exchanger 9 is separated by a gas-liquid separator, and the liquid phase refrigerant is merged into the return flow path 5 via the throttle flow path 11.
It is also possible to adopt a configuration in which the gas phase refrigerant is guided to the second heat exchanger 12.

第2熱交換器12により得られた低温の冷媒
は、キヤピラリチユーブからなる絞り流路14に
より減圧膨張されて冷却器15に送られ、そこで
少なくとも部分的に蒸発して気化熱を奪い、低温
冷却作用を行なう。
The low-temperature refrigerant obtained by the second heat exchanger 12 is expanded under reduced pressure by the throttle passage 14 made of a capillary tube, and is sent to the cooler 15, where it is at least partially evaporated to remove the heat of vaporization, resulting in a low temperature. Provides a cooling effect.

このようにして圧縮機1で圧縮された混合冷媒
が、一連の凝縮段階において放熱して順次、部分
的に凝縮されることによつて極めて低温が達成さ
れ、この極低温において冷凍冷却作用が行なわれ
る。冷却器15において冷却作用後の冷媒は、帰
還流路5を通じて圧縮機1に戻される。
The mixed refrigerant thus compressed in the compressor 1 releases heat in a series of condensation stages and is successively partially condensed to achieve an extremely low temperature, and at this extremely low temperature the refrigeration cooling action takes place. It can be done. The refrigerant after cooling in the cooler 15 is returned to the compressor 1 through the return flow path 5.

一方、気液分離器7による圧縮機潤滑油の分離
が100%完全でなく、若干ではあるが低温域への
漏洩があるため、これが低温状態において流動し
なくなり、配管内に蓄積される。この場合、特に
径の細いキヤピラリチユーブから成る絞り流路1
1,14では管閉塞の危険性があり、この傾向は
最低温域の絞り流路14において最も顕著であ
り、またその他の配管部でも冷媒の輸送効率が悪
くなるなどの問題が生じる。
On the other hand, the separation of the compressor lubricating oil by the gas-liquid separator 7 is not 100% complete, and there is some leakage into the low-temperature region, so this oil does not flow in the low-temperature state and accumulates in the pipes. In this case, the throttle channel 1 consists of a capillary tube with a particularly small diameter.
1 and 14, there is a risk of pipe clogging, and this tendency is most noticeable in the throttle channel 14 in the lowest temperature range, and problems such as poor refrigerant transport efficiency also occur in other piping sections.

そこでこの考案では、気液分離器7から、最低
温域の絞り流路14の直上流側に至るバイパス流
路16を設け、このバイパス流路16に電磁弁1
7を介挿して開閉自在としている。そして電磁弁
17を開けることにより、気液分離器7において
分離された比較的高温の液相冷媒を絞り流路14
の入口付近にバイパスして流し、絞り流路14を
洗浄することが可能なように構成している。
Therefore, in this invention, a bypass flow path 16 is provided from the gas-liquid separator 7 to the immediately upstream side of the throttle flow path 14 in the lowest temperature range, and a solenoid valve 1 is provided in this bypass flow path 16.
7 is inserted so that it can be opened and closed freely. By opening the solenoid valve 17, the relatively high temperature liquid refrigerant separated in the gas-liquid separator 7 is throttled into the flow path 14.
The filter is configured so that it can be bypassed and flowed near the inlet of the filter to clean the throttle channel 14.

例えば定期的(12時間または24時間毎)に電磁
弁17を数分間開けて、絞り流路14内に付着し
た圧縮機潤滑油を洗浄することにより、長期にお
ける連続運転でも管閉塞は生じず、冷却性能を低
下させることもない。その間の温度上昇は3〜5
℃程度であり、実用上さしつかえないものであ
る。気液分離器7により分離されたR11,R1
2等の液相冷媒は圧縮機潤滑油との溶解性に優
れ、圧縮機潤滑油の洗浄に対する効果は大きい。
またこの液相冷媒の温度は絞り流路14付近より
もかなり高く、電磁弁17を開けてバイパスさせ
ることにより絞り流路14付近の温度を上げるこ
とができるので、付着した圧縮機潤滑油の流動性
を良くすることができ、洗浄効果は一層高まる。
For example, by opening the solenoid valve 17 for several minutes periodically (every 12 or 24 hours) to clean the compressor lubricating oil that has adhered to the inside of the throttle channel 14, pipe blockage will not occur even during long-term continuous operation. There is no reduction in cooling performance. The temperature rise during that time is 3-5
℃, which is not a practical problem. R11 and R1 separated by gas-liquid separator 7
Liquid phase refrigerants such as No. 2 have excellent solubility in compressor lubricating oil and are highly effective in cleaning compressor lubricating oil.
In addition, the temperature of this liquid phase refrigerant is considerably higher than that near the throttle channel 14, and by opening the solenoid valve 17 and bypassing it, the temperature near the throttle channel 14 can be raised. The cleaning effect can be further enhanced.

なお上記実施例では、絞り流路14の直上流側
にバイパス流路16を接続したが、これを絞り流
路11の直上流側に接続してもよく、またその両
方に接続して電磁弁により選択的に開成するよう
に構成してもよい。また絞り流路8,11,14
としてキヤピラリチユーブを用いた例につき説明
したが、絞り弁を用いる場合にもこの考案を適用
できることは勿論である。さらに熱交換器が2段
構成の場合を示したが、より多段構成であつても
同様に適用できる。
In the above embodiment, the bypass flow path 16 is connected to the immediately upstream side of the throttle flow path 14, but it may be connected to the right upstream side of the throttle flow path 11, or it may be connected to both of them to form a solenoid valve. It may also be configured to selectively open. Also, the throttle channels 8, 11, 14
Although an example using a capillary tube has been described, it goes without saying that this invention can also be applied to a case where a throttle valve is used. Further, although the case where the heat exchanger has a two-stage configuration is shown, the present invention can be similarly applied even if the heat exchanger has a multi-stage configuration.

(考案の効果) 以上説明したように、この考案によれば、圧縮
機潤滑油を溶解した混合冷媒を用いる冷凍システ
ムにおいて、長期連続運転によつても管詰り現象
が生ずることなく、冷凍効率の低下することのな
い低温冷凍機を得ることができる。
(Effects of the invention) As explained above, according to this invention, in a refrigeration system using a mixed refrigerant in which compressor lubricating oil is dissolved, pipe clogging does not occur even during long-term continuous operation, and the refrigeration efficiency is improved. A low-temperature refrigerator that does not deteriorate can be obtained.

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

図面はこの考案による低温冷凍機の一実施例を
示す構成図である。 1……圧縮機、3……凝縮器、5……帰還流
路、7……気液分離器、8,11,14……絞り
流路、9,12……熱交換器、15……冷却器、
16……バイパス流路、17……電磁弁。
The drawing is a configuration diagram showing an embodiment of the low temperature refrigerator according to this invention. 1... Compressor, 3... Condenser, 5... Return path, 7... Gas-liquid separator, 8, 11, 14... Throttle channel, 9, 12... Heat exchanger, 15... Cooler,
16... Bypass flow path, 17... Solenoid valve.

Claims (1)

【実用新案登録請求の範囲】 (1) 圧縮機潤滑油を溶解するための比較的高沸点
の第1の冷媒を含むそれぞれ異なつた沸点を有
する複数の冷媒から成る高温気相状態の混合冷
媒を圧縮するための圧縮機と、 前記混合冷媒を前記圧縮機に導入する帰還流
路と、 前記圧縮機で圧縮された混合冷媒を部分的に
凝縮させ、少なくとも前記第1の冷媒を液相の
状態として含んだ気液混合冷媒を作り出す凝縮
器と、 前記気液混合冷媒を気相冷媒と液相冷媒とに
分離する気液分離器と、 前記帰還流路上に設けられ、前記気液分離器
により分離された気相冷媒を、前記帰還流路を
流れる冷媒との熱交換により少なくとも部分的
に凝縮させて、低温の液相もしくは気液混合冷
媒を作り出す複数の熱交換器と、 前記気液分離器により分離された液相冷媒を
減圧膨張させ、この減圧膨張させた液相冷媒
を、前記熱交換器のうち帰還流路の最上流側に
位置する熱交換器を除く所定の熱交換器の直上
流において前記帰還流路に合流させる第1の絞
り流路と、 前記第1の絞り流路との合流点より前記帰還
流路上において下流側に位置する熱交換器によ
る部分凝縮により得られた液相冷媒を減圧膨張
させて、前記第1の絞り流路よりも前記帰還流
路上において上流側に位置する熱交換器の直上
流で前記帰還流路に合流させる第2の絞り流路
と、 前記第1の絞り流路よりも前記帰還流路上に
おいて上流側に位置する熱交換器により得られ
た低温液相冷媒を減圧膨張させる第3の絞り流
路と、 前記第3の絞り流路により減圧膨張された低
温液相冷媒を少なくとも部分的に蒸発させるこ
とにより低温冷却し、前記帰還流路の上流端に
導入する冷却器と、 を備える低温冷凍機において、 前記気液分離器により気相冷媒と分離された
液相冷媒を、前記第2の絞り流路または第3の
絞り流路のうちの少なくとも一の絞り流路の直
上流に合流させるバイパス流路と、 このバイパス流路を開閉する開閉手段と、 をさらに備えることを特徴とする低温冷凍機。 (2) 前記第2、第3の絞り流路はキヤピラリチユ
ーブである、実用新案登録請求の範囲第1項記
載の低温冷凍機。
[Claims for Utility Model Registration] (1) A mixed refrigerant in a high temperature vapor phase consisting of a plurality of refrigerants each having a different boiling point, including a first refrigerant with a relatively high boiling point for dissolving compressor lubricating oil. a compressor for compressing; a return flow path for introducing the mixed refrigerant into the compressor; and a return flow path for partially condensing the mixed refrigerant compressed by the compressor to bring at least the first refrigerant into a liquid phase. a condenser that produces a gas-liquid mixed refrigerant containing the gas-liquid refrigerant; a gas-liquid separator that separates the gas-liquid mixed refrigerant into a gas-phase refrigerant and a liquid-phase refrigerant; a plurality of heat exchangers that at least partially condense the separated gas-phase refrigerant through heat exchange with the refrigerant flowing through the return flow path to produce a low-temperature liquid phase or gas-liquid mixed refrigerant; and the gas-liquid separation. The liquid phase refrigerant separated by the chamber is expanded under reduced pressure, and the expanded liquid phase refrigerant is transferred to a predetermined heat exchanger other than the heat exchanger located on the most upstream side of the return flow path among the heat exchangers. A first throttle channel that joins the return channel immediately upstream; and a heat exchanger located downstream of the junction with the first throttle channel on the return channel. a second throttle flow path that expands the liquid phase refrigerant under reduced pressure and joins the return flow path immediately upstream of a heat exchanger located upstream of the return flow path than the first throttle flow path; a third throttle flow path for depressurizing and expanding a low-temperature liquid phase refrigerant obtained by a heat exchanger located upstream of the return flow path than the first throttle flow path; and by the third throttle flow path. A low-temperature refrigerator comprising: a cooler that cools the low-temperature liquid phase refrigerant that has been expanded under reduced pressure by at least partially evaporating it and introduces it into the upstream end of the return flow path; a bypass flow path in which the liquid phase refrigerant separated from the refrigerant joins immediately upstream of at least one of the second throttle flow path or the third throttle flow path; and opening and closing of this bypass flow path. A low-temperature refrigerator further comprising an opening/closing means for opening and closing the refrigerator. (2) The low temperature refrigerator according to claim 1, wherein the second and third throttle channels are capillary tubes.
JP1986177329U 1986-11-18 1986-11-18 Expired - Lifetime JPH0541320Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1986177329U JPH0541320Y2 (en) 1986-11-18 1986-11-18

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1986177329U JPH0541320Y2 (en) 1986-11-18 1986-11-18

Publications (2)

Publication Number Publication Date
JPS6382171U JPS6382171U (en) 1988-05-30
JPH0541320Y2 true JPH0541320Y2 (en) 1993-10-19

Family

ID=31118433

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1986177329U Expired - Lifetime JPH0541320Y2 (en) 1986-11-18 1986-11-18

Country Status (1)

Country Link
JP (1) JPH0541320Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57163562U (en) * 1981-04-10 1982-10-15

Also Published As

Publication number Publication date
JPS6382171U (en) 1988-05-30

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