JP2711878B2 - Low temperature refrigeration equipment - Google Patents

Low temperature refrigeration equipment

Info

Publication number
JP2711878B2
JP2711878B2 JP1009967A JP996789A JP2711878B2 JP 2711878 B2 JP2711878 B2 JP 2711878B2 JP 1009967 A JP1009967 A JP 1009967A JP 996789 A JP996789 A JP 996789A JP 2711878 B2 JP2711878 B2 JP 2711878B2
Authority
JP
Japan
Prior art keywords
refrigerant
temperature
load cooler
low
heat exchanger
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
Application number
JP1009967A
Other languages
Japanese (ja)
Other versions
JPH02192545A (en
Inventor
文夫 栗山
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP1009967A priority Critical patent/JP2711878B2/en
Publication of JPH02192545A publication Critical patent/JPH02192545A/en
Application granted granted Critical
Publication of JP2711878B2 publication Critical patent/JP2711878B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は圧縮機を用いた冷凍装置、特に複数種の非共
沸混合冷媒を用いて低温を得るための冷凍装置に関す
る。
Description: TECHNICAL FIELD The present invention relates to a refrigeration apparatus using a compressor, and more particularly to a refrigeration apparatus for obtaining a low temperature using a plurality of types of non-azeotropic refrigerant mixtures.

〔従来の技術〕[Conventional technology]

混合冷凍サイクルは、混合冷媒を段階的に高沸点冷媒
順に液化分離させ、断熱膨張させることにより、順次低
沸点冷媒を凝縮させて低温を得ることができるものであ
る。
In the mixed refrigeration cycle, the mixed refrigerant is liquefied and separated step by step in the order of the high-boiling refrigerant and is adiabatically expanded, whereby the low-boiling refrigerant can be sequentially condensed to obtain a low temperature.

公知の混合冷凍サイクルを第2図を用いて説明する。
第2図においては、混合冷媒を圧縮機1により断熱圧縮
し、この断熱圧縮冷媒を凝縮器2にて冷却水等により冷
却し、部分的に凝縮させ、この気液混合冷媒を補助熱交
換器3にて低温部からのもどり冷媒と熱交換させ、更に
部分凝縮させた後、第1分離器4にて凝縮冷媒と未凝縮
冷媒とに分離させる。分離された凝縮冷媒は第1膨張弁
5にて断熱膨張させることにより低温を発生させ、低温
部からのもどり冷媒と合流させ、第1熱交換器6に流通
させ、第1分離器にて分離した未凝縮冷媒を更に冷却
し、部分的に凝縮させる。これを順次くり返すことによ
り、順次低い沸点の冷媒を凝縮させ、これを断熱膨張さ
せることにより、より低温の冷媒ガスを発生させること
ができる。
A known mixed refrigeration cycle will be described with reference to FIG.
In FIG. 2, the mixed refrigerant is adiabatically compressed by a compressor 1, and the adiabatic compressed refrigerant is cooled by cooling water or the like in a condenser 2 and partially condensed. At 3, heat is exchanged with the return refrigerant from the low-temperature part, and after being partially condensed, the first separator 4 separates the refrigerant into condensed refrigerant and uncondensed refrigerant. The separated condensed refrigerant is adiabatically expanded by the first expansion valve 5 to generate a low temperature, merges with the return refrigerant from the low temperature part, flows through the first heat exchanger 6, and is separated by the first separator. The uncondensed refrigerant thus cooled is further cooled and partially condensed. By sequentially repeating this, the refrigerant having a lower boiling point is sequentially condensed and adiabatically expanded, whereby a lower-temperature refrigerant gas can be generated.

また上記の混合冷凍サイクルにおいて、低温冷媒と高
温冷媒とを切り替え供給する公知(米国特許第4,535,59
7号明細書)の方法を第3図を用いて説明する。冷凍サ
イクルについては、第2図を用いて前述された通りであ
る。負荷冷却器14には低温冷媒を流す低温冷媒コイル21
と高温冷媒を通す高温冷媒コイル22とを設ける。第1分
離器4で液化冷媒と冷凍機油とを分離排除した冷媒ガス
を圧縮機1の吐出側に設けた高温熱交換器23に導き、断
熱圧縮された高温の送り冷媒16と熱交換させ、前記高温
冷媒コイル22に流す。低温冷媒・高温冷媒を供給する流
路には開閉弁19,20を各々設け、切り替え運転する。
Also, in the above-mentioned mixed refrigeration cycle, a low-temperature refrigerant and a high-temperature refrigerant are switched and supplied (US Pat. No. 4,535,595).
The method of No. 7 is described with reference to FIG. The refrigeration cycle is as described above with reference to FIG. A low-temperature refrigerant coil 21 for flowing a low-temperature refrigerant to the load cooler 14
And a high-temperature refrigerant coil 22 for passing high-temperature refrigerant. The refrigerant gas from which the liquefied refrigerant and the refrigerating machine oil have been separated and eliminated by the first separator 4 is led to a high-temperature heat exchanger 23 provided on the discharge side of the compressor 1 and heat-exchanged with the adiabatic-compressed high-temperature feed refrigerant 16, The high-temperature refrigerant coil 22 flows. Opening / closing valves 19 and 20 are provided in the flow paths for supplying the low-temperature refrigerant and the high-temperature refrigerant, respectively, to perform a switching operation.

更に、もう一つの公知(米国特許第4,597,267号明細
書)の方法を第4図を用いて説明すると、低温冷媒供給
サイクルについては第2図を用いて前述した通りであ
る。高温冷媒供給サイクルについて第4図を用いて説明
する。低温冷媒供給弁を閉じ、高温冷媒供給弁を開け、
最終分離器10を出た冷媒ガスを低温熱交換器24にて冷媒
もどりガスと熱交換させた後、圧縮機1の吐出側の断熱
圧縮された高温冷媒と高温熱交換機23にて熱交換させ昇
温させた後、負荷冷却器14に供給する。このようにし
て、低温冷媒と高温冷媒とを切替供給する。
Further, another known method (U.S. Pat. No. 4,597,267) will be described with reference to FIG. 4. The low-temperature refrigerant supply cycle is as described above with reference to FIG. The high-temperature refrigerant supply cycle will be described with reference to FIG. Close the low-temperature refrigerant supply valve, open the high-temperature refrigerant supply valve,
After the refrigerant gas that has exited the final separator 10 undergoes heat exchange with the refrigerant return gas in the low-temperature heat exchanger 24, heat exchange is performed with the adiabatic-compressed high-temperature refrigerant on the discharge side of the compressor 1 and the high-temperature heat exchanger 23. After the temperature is raised, it is supplied to the load cooler 14. In this way, the low-temperature refrigerant and the high-temperature refrigerant are switched and supplied.

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

前述のような混合冷媒冷凍サイクルにおいては、低温
冷媒供給サイクルから高温冷媒供給サイクルに切替えた
とき、低温に冷却された各熱交換器内に高温冷媒が流
れ、液化されていた冷媒を急速に気化させ、機内圧力を
異常上昇させてしまう。このため、機内のガス流れが閉
そくし、圧縮機吐出圧が異常上昇し、圧縮機が過負荷状
態となり運転を継続できなくなることがある。このた
め、通常、高温冷媒供給サイクルは1分ないし2分程度
に制限せざるを得ない。
In the mixed refrigerant refrigeration cycle described above, when switching from the low-temperature refrigerant supply cycle to the high-temperature refrigerant supply cycle, the high-temperature refrigerant flows in each heat exchanger cooled to low temperature, and the liquefied refrigerant is rapidly vaporized. And the internal pressure rises abnormally. For this reason, the gas flow in the machine may be blocked, the discharge pressure of the compressor may rise abnormally, and the compressor may be overloaded, and the operation may not be continued. For this reason, the high-temperature refrigerant supply cycle usually has to be limited to about 1 to 2 minutes.

また、圧縮機および凝縮器等の常温部と、中間熱交換
器および分離器等の低温部とを分離し設置する場合、低
温部側にある冷媒ガスを常温部側にある高温熱交換器ま
で導き、また、低温部側にある負荷冷却器まで送る配管
施工が必要となる。これは施工上大きな負担となるばか
りでなく、冷媒循環の圧力損失にもなり、圧縮機に大き
な負担をかけることになる。
When a normal temperature section such as a compressor and a condenser is separated from a low temperature section such as an intermediate heat exchanger and a separator, the refrigerant gas in the low temperature section is transferred to the high temperature heat exchanger in the normal temperature section. It is necessary to construct a pipe for guiding and sending it to the load cooler on the low temperature part side. This not only imposes a heavy burden on the construction, but also causes a pressure loss in the refrigerant circulation, and places a heavy burden on the compressor.

そこで、本発明は、上記のような課題を解決し、配管
施工が比較的簡単で、低温冷媒と高温冷媒を容易に切替
でき、長時間運転しても装置に負担のかからない冷凍装
置を提供することを目的とする。
Therefore, the present invention provides a refrigeration system that solves the above-described problems, has relatively simple piping construction, can easily switch between a low-temperature refrigerant and a high-temperature refrigerant, and does not burden the device even when operated for a long time. The purpose is to:

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

上記の目的は、最終段の減圧弁を介して最低温の冷媒
を負荷冷却器に流通させる第1冷媒供給流路と、これと
並行して、中間熱交換器の送り冷媒側より比較的高温の
冷媒を負荷冷却器に流通させる第2冷媒供給流路とを設
け、各々の冷媒供給流路に開閉弁を設けて、最低温冷媒
と比較的高温冷媒とを切替供給することにより達成され
る。
The above-described object is to provide a first refrigerant supply passage through which the lowest-temperature refrigerant flows through the load cooler through the final-stage pressure reducing valve, and, in parallel with this, a relatively high temperature from the sending refrigerant side of the intermediate heat exchanger. And a second refrigerant supply passage for allowing the refrigerant to flow through the load cooler, and providing an on-off valve in each refrigerant supply passage to switch and supply the lowest temperature refrigerant and the relatively high temperature refrigerant. .

すなわち、本発明は、圧縮機、凝縮器、負荷冷却器、
該圧縮機吐出側の送り冷媒と該負荷冷却器からのもどり
冷媒とを流通する複数段の中間熱交換器、複数の分離器
と減圧器を具備し、冷媒には複数種の非共沸混合冷媒を
用い、該凝縮器を経た冷媒の凝縮冷媒を分離器で分離
し、該減圧器を介して負荷冷却器を経たより低温度から
のもどり冷媒と合流し、該中間熱交換器の未凝縮冷媒を
冷却し、順次低い沸点の冷媒を凝縮せしめて、凝縮冷媒
を該減圧器を介して該負荷冷却器に流通することにより
低温を得る冷凍装置において、最終段の減圧器を介して
最低温の冷媒を該負荷冷却器に流通せしめる第1冷媒供
給流路と、前記の最終段の減圧器を介さず、該中間熱交
換器より比較的高温の冷媒を、途中の熱交換器で熱交換
することなく負荷冷却器に流通せしめる第2冷媒供給流
路とを設け、該第1冷媒供給流路及び該第2冷媒供給流
路に各々開閉弁を設け、前記最低温の冷媒と比較的高温
の冷媒とを切り換えて、該負荷冷却器に供給できるよう
にした冷凍装置にある。
That is, the present invention provides a compressor, a condenser, a load cooler,
A plurality of stages of intermediate heat exchangers, in which a feed refrigerant on the compressor discharge side and a return refrigerant from the load cooler flow, a plurality of separators and a decompressor, and a plurality of types of non-azeotropic mixing Using a refrigerant, the condensed refrigerant of the refrigerant that has passed through the condenser is separated by a separator, merges with the return refrigerant from a lower temperature that has passed through the load cooler through the decompressor, and has not been condensed in the intermediate heat exchanger. In a refrigeration system that cools a refrigerant and sequentially condenses a refrigerant having a lower boiling point and circulates the condensed refrigerant to the load cooler through the decompressor, the lowest temperature is supplied through a final stage decompressor. And a first refrigerant supply passage through which the refrigerant flows through the load cooler, and heat exchange between the refrigerant having a relatively higher temperature than the intermediate heat exchanger and the intermediate heat exchanger without passing through the final stage decompressor. And a second refrigerant supply channel for flowing through the load cooler without performing Each on-off valve provided in the medium supply channel and the second coolant supply passage, the switching between a relatively high-temperature refrigerant and coldest refrigerant in refrigeration apparatus which can supply to the load cooler.

〔作 用〕(Operation)

本発明の低温冷凍装置を用いれば、負荷冷却器に最低
温度冷媒と比較的高温の低温冷媒とを容易に切替え供給
することができる。また、供給冷媒温度切替に伴なう圧
縮機の過負荷状態になることもなく、安定した運転を行
なうことができる。
By using the low-temperature refrigeration apparatus of the present invention, the lowest temperature refrigerant and the relatively high-temperature low-temperature refrigerant can be easily switched and supplied to the load cooler. In addition, stable operation can be performed without the compressor being overloaded due to the switching of the supply refrigerant temperature.

〔実施例〕〔Example〕

以下に、本発明の実施例を図面を用いて説明するが、
本発明はこれら実施例に限定されるものではない。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
The present invention is not limited to these examples.

実施例1 低温冷媒と比較的高温の冷媒とを切替供給する、非共
沸混合冷媒を用いた低温冷凍装置を第1図に示す。混合
冷媒を圧縮機1により断熱圧縮し、この断熱圧縮冷媒を
凝縮機2にて冷却水等により冷却し、部分的に凝縮さ
せ、この気液混合冷媒を補助熱交換器3にて低温部から
のもどり冷媒と熱交換させ、更に部分凝縮を進行させ、
第1分離器4にて凝縮冷媒と未凝縮冷媒とを分離させ
る。分離された凝縮冷媒は、第1膨張弁5にて断熱膨強
させることにより低温を発生させ、低温部からのもどり
冷媒と合流させ、第1熱交換器6に流通させ、第1分離
器にて分離した未凝縮冷媒を更に冷却し、部分的に凝縮
させる。これを順次くり返すことにより低温を得ること
ができる。
Example 1 FIG. 1 shows a low-temperature refrigeration system using a non-azeotropic refrigerant mixture for switchingly supplying a low-temperature refrigerant and a relatively high-temperature refrigerant. The mixed refrigerant is adiabatically compressed by the compressor 1, the adiabatic compressed refrigerant is cooled by cooling water or the like in the condenser 2 and partially condensed, and the gas-liquid mixed refrigerant is cooled by the auxiliary heat exchanger 3 from the low-temperature portion. Heat exchange with the return refrigerant, further promote partial condensation,
The first separator 4 separates the condensed refrigerant from the uncondensed refrigerant. The separated condensed refrigerant generates a low temperature by being adiabatically expanded by the first expansion valve 5, merges with the return refrigerant from the low temperature part, flows through the first heat exchanger 6, and passes through the first separator. The separated uncondensed refrigerant is further cooled and partially condensed. By repeating this in sequence, a low temperature can be obtained.

最も低温を得ようとする場合は、低温冷媒供給電磁弁
19を開け、高温冷媒供給電磁弁20を閉じ、前述冷凍サイ
クルにより、冷媒を最終段膨張弁13を通し、冷温冷媒を
負荷冷却器14に供給する。また、比較的高温の冷媒を得
ようとする場合は、高温冷媒供給電磁弁20を開け、低温
冷媒供給電磁弁19を閉じ、前述冷凍サイクルの途中段よ
り冷媒を負荷冷却器14に供給する。このようにして、電
磁弁の切替により、低温の冷媒供給と比較的高温の冷媒
供給とを切替供給することができる。
To get the lowest temperature, use a low-temperature refrigerant supply solenoid valve.
19 is opened, the high-temperature refrigerant supply solenoid valve 20 is closed, and the refrigerant is supplied to the load cooler 14 through the last-stage expansion valve 13 by the refrigeration cycle. When a relatively high-temperature refrigerant is to be obtained, the high-temperature refrigerant supply solenoid valve 20 is opened, the low-temperature refrigerant supply solenoid valve 19 is closed, and the refrigerant is supplied to the load cooler 14 from an intermediate stage of the refrigeration cycle. In this manner, by switching the solenoid valve, it is possible to switch and supply between a low-temperature refrigerant supply and a relatively high-temperature refrigerant supply.

そして、本冷凍装置を真空排気装置に用いれば、凍結
排気及び再生を好適に行なうことができる。
Then, when the present refrigeration apparatus is used for a vacuum exhaust device, freezing and exhausting and regeneration can be suitably performed.

〔発明の効果〕〔The invention's effect〕

本発明の低温冷凍装置によれば、配管施工が比較的簡
単で、低温冷媒と高温冷媒とを容易に切替えて運転で
き、長時間運転しても装置に負担がかからない。
ADVANTAGE OF THE INVENTION According to the low-temperature refrigeration apparatus of this invention, piping construction is comparatively easy, a low-temperature refrigerant | coolant and a high-temperature refrigerant | coolant can be switched easily, and operation | movement is possible, and even if it operates for a long time, a load is not put on an apparatus.

また、この低温冷凍装置の負荷冷却部を真空排気装置
に組み込んで真空排気を行えば、連続的に冷却面の再生
を行なうことができる。
Further, if the load cooling section of the low-temperature refrigeration apparatus is incorporated into a vacuum exhaust device and the vacuum exhaust is performed, the cooling surface can be continuously regenerated.

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

第1図は本発明の一実施例を示す経路図、第2図、第3
図、第4図は公知の低温冷凍装置を示す経路図である。 1……圧縮機、2……凝縮器、3……補助熱交換器、4
……第1分離器、5……第1膨張弁、6……第1熱交換
器、7……第2分離器、8……第2膨張弁、9……第2
熱交換器、10……第3分離器、11……第3膨張弁、12…
…第3熱交換器、13……最終段膨張弁、14……負荷冷却
器、15……タンク、16……送り冷媒、17……もどり冷
媒、18……第4膨張弁、19……低温冷媒供給電磁弁、20
……高温冷媒供給電磁弁、21……低温冷媒供給配管、22
……高温冷媒供給配管、
FIG. 1 is a route diagram showing one embodiment of the present invention, FIG.
FIG. 4 is a route diagram showing a known low-temperature refrigeration apparatus. 1 ... Compressor, 2 ... Condenser, 3 ... Auxiliary heat exchanger, 4
... 1st separator, 5 ... 1st expansion valve, 6 ... 1st heat exchanger, 7 ... 2nd separator, 8 ... 2nd expansion valve, 9 ... 2nd
Heat exchanger, 10 third separator, 11 third expansion valve, 12
... 3rd heat exchanger, 13 ... last stage expansion valve, 14 ... load cooler, 15 ... tank, 16 ... sending refrigerant, 17 ... returning refrigerant, 18 ... 4th expansion valve, 19 ... Low temperature refrigerant supply solenoid valve, 20
…… High temperature refrigerant supply solenoid valve, 21 …… Low temperature refrigerant supply piping, 22
…… High-temperature refrigerant supply piping,

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】圧縮機、凝縮器、負荷冷却器、該圧縮機吐
出側の送り冷媒と該負荷冷却器からのもどり冷媒とを流
通する複数段の中間熱交換器、複数の分離器と減圧器を
具備し、冷媒には複数種の非共沸混合冷媒を用い、該凝
縮器を経た冷媒の凝縮冷媒を分離器で分離し、該減圧器
を介して負荷冷却器を経たより低温部からのもどり冷媒
と合流し、該中間熱交換器の未凝縮冷媒を冷却し、順次
低い沸点の冷媒を凝縮せしめて、凝縮冷媒を該減圧器を
介して該負荷冷却器に流通することにより低温を得る冷
凍装置において、最終段の減圧器を介して再低温の冷媒
を該負荷冷却器に流通せしめる第1冷媒供給流路と、前
記の最終段の減圧器を介さず、該中間熱交換器より比較
的高温の冷媒を、途中の熱交換器で熱交換することなく
負荷冷却器に流通せしめる第2冷媒供給流路とを設け、
該第1冷媒供給流路及び該第2冷媒供給流路に各々開閉
弁を設け、前記最低温の冷媒と比較的高温の冷媒とを切
り換えて該負荷冷却器に供給できるようにした冷凍装
置。
1. A compressor, a condenser, a load cooler, a plurality of intermediate heat exchangers for passing a refrigerant sent from the compressor discharge side and a return refrigerant from the load cooler, a plurality of separators, and a decompression device. Equipped with a plurality of types of non-azeotropic refrigerant mixture, the condensed refrigerant of the refrigerant passed through the condenser is separated by a separator, from the lower temperature portion passed through the load cooler through the decompressor Return refrigerant, cools the uncondensed refrigerant in the intermediate heat exchanger, sequentially condenses the refrigerant having a lower boiling point, and circulates the condensed refrigerant to the load cooler through the decompressor to reduce the low temperature. In the refrigeration apparatus to be obtained, a first refrigerant supply flow path through which the re-low temperature refrigerant flows to the load cooler through the final stage decompressor, and the intermediate heat exchanger without the intermediary of the final stage decompressor Relatively high-temperature refrigerant flows to the load cooler without exchanging heat in intermediate heat exchangers And a second refrigerant supply channel occupying provided,
A refrigeration system in which an opening / closing valve is provided in each of the first refrigerant supply flow path and the second refrigerant supply flow path so that the lowest temperature refrigerant and a relatively high temperature refrigerant can be switched and supplied to the load cooler.
JP1009967A 1989-01-20 1989-01-20 Low temperature refrigeration equipment Expired - Lifetime JP2711878B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1009967A JP2711878B2 (en) 1989-01-20 1989-01-20 Low temperature refrigeration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1009967A JP2711878B2 (en) 1989-01-20 1989-01-20 Low temperature refrigeration equipment

Publications (2)

Publication Number Publication Date
JPH02192545A JPH02192545A (en) 1990-07-30
JP2711878B2 true JP2711878B2 (en) 1998-02-10

Family

ID=11734701

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1009967A Expired - Lifetime JP2711878B2 (en) 1989-01-20 1989-01-20 Low temperature refrigeration equipment

Country Status (1)

Country Link
JP (1) JP2711878B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004510944A (en) * 2000-10-05 2004-04-08 オペロン・カンパニー・リミテッド Cryogenic refrigeration system
CN109357428A (en) * 2018-08-30 2019-02-19 青岛诺诚化学品安全科技有限公司 A kind of three-level self-overlay refrigerating device for device for recovering oil and gas

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63263360A (en) * 1987-04-20 1988-10-31 株式会社東洋製作所 Refrigerator

Also Published As

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JPH02192545A (en) 1990-07-30

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