JPH0443261A - Freezing device - Google Patents

Freezing device

Info

Publication number
JPH0443261A
JPH0443261A JP14793390A JP14793390A JPH0443261A JP H0443261 A JPH0443261 A JP H0443261A JP 14793390 A JP14793390 A JP 14793390A JP 14793390 A JP14793390 A JP 14793390A JP H0443261 A JPH0443261 A JP H0443261A
Authority
JP
Japan
Prior art keywords
stage compressor
refrigerant
low
temperature
pressure
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
JP14793390A
Other languages
Japanese (ja)
Inventor
Masao Kimura
木村 誠夫
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric 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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP14793390A priority Critical patent/JPH0443261A/en
Publication of JPH0443261A publication Critical patent/JPH0443261A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/13Economisers

Abstract

PURPOSE:To prevent heating of a low stage compressor and to improve reliability by a method wherein a high temperature high pressure refrigerant gas discharged from a high stage compressor is liquefied by a condenser and subcooled and discharged to a condenser and an intermediate cooler to branch a part thereof to the liquid injection port of the low stage compressor is provided. CONSTITUTION:Refrigerant gas discharged from a high stage compressor 2 is liquefied by a condenser 3 and subcooled and discharged to a vaporizer 5, and an intermediate cooler 9 branches a part thereof to a liquid injection port 10 of a low stage compressor 1. A refrigerant from a vaporizer 5 is compressed by a low stage compressor 1, a discharge gas temperature is increased and sucked to a high stage compressor 2 together with a refrigerant the temperature of which is reduced through liquid injection. In which case, a pressure in the injection port 10 is kept at a value between an intermediate and a middle pressure, and since the pressure of a liquid refrigerant is high, liquid injection is always effected by means of a pressure difference. By controlling an intermediate expansion valve 8 so that a low stage discharge gas temperature is adjusted to +5-+20 deg.C, temperature is adjusted to a value at which enough operation is carried out at the high stage compressor 2 also.

Description

【発明の詳細な説明】 〔産業上の利用分野] この発明は、低段圧縮機に圧縮工程の途中に液インジェ
クションを行う圧縮機を有する二段の圧縮式冷凍装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a two-stage compression refrigeration system having a compressor that injects liquid into a lower stage compressor during the compression process.

〔従来の技術〕[Conventional technology]

第2回は例えば実開昭54−17255号公報に示され
た従来の二段圧縮式冷凍装置を示す冷媒回路図であり、
図中の18は低段圧縮機、2は高段圧縮機、3は凝縮器
、4は膨張弁、5は蒸発器、6は電磁弁であり、また、
9は中間冷却器であり、液冷媒を冷却した後、中間アキ
ュムレータ11に接続される。
The second part is a refrigerant circuit diagram showing a conventional two-stage compression type refrigeration device shown in, for example, Japanese Utility Model Application Publication No. 54-17255,
In the figure, 18 is a low-stage compressor, 2 is a high-stage compressor, 3 is a condenser, 4 is an expansion valve, 5 is an evaporator, and 6 is a solenoid valve.
9 is an intercooler, which is connected to the intermediate accumulator 11 after cooling the liquid refrigerant.

これらの低段圧縮機1a、中間アキュムレータ11、高
段圧縮機2、凝縮器3、中間冷却器9、電磁弁6、膨張
弁4、蒸発器5は管路で連結され、冷媒回路を構成して
いる。
These low-stage compressor 1a, intermediate accumulator 11, high-stage compressor 2, condenser 3, intercooler 9, solenoid valve 6, expansion valve 4, and evaporator 5 are connected by a pipe line and constitute a refrigerant circuit. ing.

また、7は中間電磁弁、8は中間膨張弁であり、凝li
i器3の吐出側と中間冷却器9の中間部との間に連結さ
れた管路に挿入されている。
Further, 7 is an intermediate solenoid valve, 8 is an intermediate expansion valve, and
It is inserted into a pipe line connected between the discharge side of the i-cooler 3 and the intermediate part of the intercooler 9.

次に動作ム二ついて説明する。低段圧縮機1aで吸入圧
縮された高温の冷媒は中間アキュムレータ11に流入し
、そこで中間冷却器9からの液冷媒と混合され、低温の
冷媒となり、高段圧縮機2へ吸入、圧縮され、凝縮器3
で液化され、一部は中間電磁弁7に分流されて中間膨張
弁8より中間冷却器9を経て上記中間アキュムレータ1
1に入る。
Next, I will explain the two operations. The high-temperature refrigerant sucked and compressed by the low-stage compressor 1a flows into the intermediate accumulator 11, where it is mixed with the liquid refrigerant from the intercooler 9 to become a low-temperature refrigerant, which is sucked into the high-stage compressor 2 and compressed. Condenser 3
A part of the liquid is liquefied in the intermediate electromagnetic valve 7, and is passed through the intermediate expansion valve 8, the intermediate cooler 9, and the intermediate accumulator 1.
Enter 1.

中間冷却器9で過冷却された冷媒は電磁弁6を経て膨張
弁4により減圧され、蒸発器5により蒸発して、低段圧
縮機1へ戻る。
The refrigerant supercooled in the intercooler 9 passes through the electromagnetic valve 6, is reduced in pressure by the expansion valve 4, is evaporated in the evaporator 5, and returns to the low stage compressor 1.

〔発明が解決しようとする!II!!り従来の冷凍装置
は以上のように構成されているので、低段圧縮機1aの
高温の吐出ガスを中間冷却器9を出た冷媒と中間アキュ
ムレータ11で混合するため、中間アキュムレータ11
が必要となり、また、低蒸発温度においては、低段圧縮
機la自体が過熱し、圧縮機の焼付けなどが発生するお
それがあった。
[Invention tries to solve! II! ! Since the conventional refrigeration system is configured as described above, the high temperature discharge gas of the low stage compressor 1a is mixed with the refrigerant exiting the intercooler 9 in the intermediate accumulator 11.
In addition, at low evaporation temperatures, there was a risk that the low stage compressor la itself would overheat, causing seizure of the compressor.

この発明は上記のような課題を解消するためになされた
もので、中間アキュムレータが不要となるとともに、低
段圧縮機の過熱をも防止でき、信転性の高い冷凍装置を
得ることを目的とする。
This invention was made to solve the above-mentioned problems, and aims to provide a refrigeration system that eliminates the need for an intermediate accumulator, prevents overheating of the low-stage compressor, and has high reliability. do.

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

この発明に係る冷凍装置は、低段圧縮機に吸入行程の途
中に液インジェクションできる圧縮機を採用したもので
ある。
The refrigeration system according to the present invention employs a compressor capable of injecting liquid during the suction stroke as a low-stage compressor.

〔作 用〕[For production]

この発明における低段圧縮機は液インジェクションによ
り低段吐出冷媒ガス温度は低段吐出圧力飽和温度の+2
0〜+40dey程度の所定の温度になって高段圧縮機
へ吸入される。
The low stage compressor in this invention uses liquid injection so that the low stage discharge refrigerant gas temperature is +2 above the low stage discharge pressure saturation temperature.
It reaches a predetermined temperature of about 0 to +40 days and is sucked into the high stage compressor.

〔実施例〕〔Example〕

以下、この発明の冷凍装置の実施例について図面に基づ
き説明する。第1図はその一実施例の冷媒回N図である
Embodiments of the refrigeration system of the present invention will be described below with reference to the drawings. FIG. 1 is a refrigerant circuit N diagram of one embodiment.

この第1図において、構成の説明に際し、第2図と同一
部分には同一符号を付して、第2図とは異なる部分を主
体に述べる。
In FIG. 1, when describing the configuration, the same parts as those in FIG. 2 are given the same reference numerals, and the parts different from those in FIG. 2 will be mainly described.

この第1図を第2図と比較しても明らかなように、第1
図では、第2図で示した中間アキュムレータ11が省略
され、低段圧縮機1と高段圧縮機2が直接連結されてお
り、この低段圧縮機1で圧縮行程の途中に液インジェク
ションが可能なスクロール圧縮機またはロークリ圧縮機
が使用されており、10は低段圧縮機1の液インジェク
ションボートである。その他の構成は第2図と同様であ
る。
As is clear from comparing Figure 1 with Figure 2,
In the figure, the intermediate accumulator 11 shown in Fig. 2 is omitted, and the low stage compressor 1 and the high stage compressor 2 are directly connected, and the low stage compressor 1 can perform liquid injection in the middle of the compression stroke. A scroll compressor or a rotary compressor is used, and 10 is a liquid injection boat of the low stage compressor 1. The other configurations are the same as in FIG. 2.

次に動作について説明する。低段圧縮機1で吸入された
蒸発器5からの冷媒は圧縮され、吐出ガス温度が上昇す
る。圧縮行程の途中に液インジェクションポート10か
ら中間冷却器9を出た液冷媒がインジェクションされる
Next, the operation will be explained. The refrigerant sucked into the low stage compressor 1 from the evaporator 5 is compressed, and the temperature of the discharged gas increases. The liquid refrigerant that has exited the intercooler 9 is injected from the liquid injection port 10 during the compression stroke.

液インジェクションにより温度が低下した冷媒は高段圧
縮機2へ吸入される。以下の動作は従来のものと同一で
ある。
The refrigerant whose temperature has been lowered by liquid injection is sucked into the high-stage compressor 2. The following operation is the same as the conventional one.

ところで、2段圧縮式冷凍機の場合、高圧、低圧、中間
圧は、 P・・・・”’r下ππ   ・・・(1)となる。
By the way, in the case of a two-stage compression refrigerator, the high pressure, low pressure, and intermediate pressure are P.

この(1)式において、 P、5.は高圧(絶対圧) P Hubsは中間圧(絶対圧) P tabsは低圧(絶対圧) である。In this formula (1), P.5. is high pressure (absolute pressure) P Hubs is intermediate pressure (absolute pressure) P tabs is low pressure (absolute pressure) It is.

蒸発温度は一50°C(R22でP L −b −= 
0 、654cg / cd a b s凝縮温度は3
5℃(R22でP H−b−= 13.6kg/cda
bsP □b、 =3.0 kg/CT1abs(R2
2で一15°C)となる。
The evaporation temperature is -50°C (P L −b −= at R22
0, 654cg/cd a bs condensing temperature is 3
5℃ (P H-b-= 13.6kg/cda at R22
bsP □b, =3.0 kg/CT1abs(R2
2 = -15°C).

低段圧縮機1のインジェクションポート10の圧力は中
間圧力と低圧の間であり、液冷媒は高圧であるため、圧
力差により常に液インジェクションされる。
The pressure at the injection port 10 of the low stage compressor 1 is between intermediate pressure and low pressure, and the liquid refrigerant is at high pressure, so liquid is always injected due to the pressure difference.

また、中間圧力飽和温度は一15℃で、液圧縮していな
い吐出ガス温度は通常飽和温度の+20dey以上であ
り、低段吐出ガス温度を±5〜+20°Cになるよう中
間膨張弁8を制御すれば、高段圧縮機2においても、十
分運転できる温度となる。
In addition, the intermediate pressure saturation temperature is -15°C, the temperature of the discharged gas that is not compressed is usually +20days or more of the saturation temperature, and the intermediate expansion valve 8 is set to keep the low stage discharged gas temperature within ±5 to +20°C. If the temperature is controlled, even the high-stage compressor 2 will have a temperature that allows sufficient operation.

[発明の効果] 以上のように、この発明によれば、低段圧縮機に圧縮行
程の途中に液インジェクションが可能なスクロールまた
はロークリ圧縮機の低段圧縮機を搭載したので、中間ア
キュムレータのような混合器が不要になるばかりでなく
、低段圧縮機の吐出ガス温度は常に低温に保たれ、圧縮
機の機械的信顧性が高くなるという効果がある。
[Effects of the Invention] As described above, according to the present invention, the low-stage compressor is equipped with a scroll or low-stage compressor that can inject liquid during the compression stroke. Not only does this eliminate the need for a large mixer, but the discharge gas temperature of the low-stage compressor is always maintained at a low temperature, which has the effect of increasing the mechanical reliability of the compressor.

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

第1図はこの発明の一実施例による冷凍装置の冷媒回路
図、第2図は従来の冷凍装置の冷媒回路図である。 1・・・低段圧縮機、2・・・高段圧縮機、3・・・凝
縮器、4・・・膨張弁、5・・・蒸発器、9・・・中間
冷却器、10・・・液インジェクションボート。 なお、図中、同一符号は同一、又は相当部分を示す。
FIG. 1 is a refrigerant circuit diagram of a refrigeration system according to an embodiment of the present invention, and FIG. 2 is a refrigerant circuit diagram of a conventional refrigeration system. DESCRIPTION OF SYMBOLS 1...Low stage compressor, 2...High stage compressor, 3...Condenser, 4...Expansion valve, 5...Evaporator, 9...Intercooler, 10...・Liquid injection boat. In addition, in the figures, the same reference numerals indicate the same or equivalent parts.

Claims (1)

【特許請求の範囲】[Claims] 圧縮工程の途中にインジェクションポートから液冷媒を
インジェクションして凝縮器から吸入される液冷媒と混
合して吐出する低段圧縮機と、この低段圧縮機から吐出
される冷媒を吸入して圧縮する高段圧縮機と、この高段
圧縮機から吐出される高温高圧の冷媒ガスを凝縮して液
化する凝縮器と、この凝縮器で液化された冷媒を過冷却
して上記蒸発器に吐出するとともに、この過冷却した冷
媒の一部を上記低段圧縮機の上記液インジェクションポ
ートに分流する中間冷却器とを備えた冷凍装置。
A low-stage compressor injects liquid refrigerant from the injection port during the compression process, mixes it with the liquid refrigerant drawn in from the condenser, and then discharges the mixture.The refrigerant discharged from the low-stage compressor is sucked in and compressed. A high-stage compressor, a condenser that condenses and liquefies the high-temperature, high-pressure refrigerant gas discharged from the high-stage compressor, and a condenser that supercools the liquefied refrigerant and discharges it to the evaporator. , and an intercooler that diverts a portion of the supercooled refrigerant to the liquid injection port of the low-stage compressor.
JP14793390A 1990-06-06 1990-06-06 Freezing device Pending JPH0443261A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14793390A JPH0443261A (en) 1990-06-06 1990-06-06 Freezing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14793390A JPH0443261A (en) 1990-06-06 1990-06-06 Freezing device

Publications (1)

Publication Number Publication Date
JPH0443261A true JPH0443261A (en) 1992-02-13

Family

ID=15441352

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14793390A Pending JPH0443261A (en) 1990-06-06 1990-06-06 Freezing device

Country Status (1)

Country Link
JP (1) JPH0443261A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6032472A (en) * 1995-12-06 2000-03-07 Carrier Corporation Motor cooling in a refrigeration system
EP1139039A1 (en) * 2000-03-27 2001-10-04 Carrier Corporation Economizer circuit enhancement
JP2003065615A (en) * 2001-08-23 2003-03-05 Daikin Ind Ltd Refrigerating machine
JP2007178042A (en) * 2005-12-27 2007-07-12 Mitsubishi Electric Corp Supercritical vapor compression type refrigerating cycle and cooling and heating air conditioning facility and heat pump hot-water supply machine using it
JP2008241069A (en) * 2007-03-26 2008-10-09 Mitsubishi Electric Corp Air conditioning device
JP2010525293A (en) * 2007-04-24 2010-07-22 キャリア コーポレイション Transcritical refrigerant vapor compression system with charge control
JP2010164291A (en) * 2008-12-15 2010-07-29 Denso Corp Ejector-type refrigeration cycle
JP2011512509A (en) * 2008-02-19 2011-04-21 キャリア コーポレイション Refrigerant vapor compression system
EP2312226A3 (en) * 2009-09-30 2014-10-29 Fujitsu General Limited Heat pump apparatus
JP2018119741A (en) * 2017-01-25 2018-08-02 ダイキン工業株式会社 Refrigerating device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS597859A (en) * 1982-07-07 1984-01-17 株式会社日立製作所 Two stage screw refrigerator

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS597859A (en) * 1982-07-07 1984-01-17 株式会社日立製作所 Two stage screw refrigerator

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6032472A (en) * 1995-12-06 2000-03-07 Carrier Corporation Motor cooling in a refrigeration system
EP1139039A1 (en) * 2000-03-27 2001-10-04 Carrier Corporation Economizer circuit enhancement
JP2003065615A (en) * 2001-08-23 2003-03-05 Daikin Ind Ltd Refrigerating machine
JP2007178042A (en) * 2005-12-27 2007-07-12 Mitsubishi Electric Corp Supercritical vapor compression type refrigerating cycle and cooling and heating air conditioning facility and heat pump hot-water supply machine using it
JP2008241069A (en) * 2007-03-26 2008-10-09 Mitsubishi Electric Corp Air conditioning device
JP2010525293A (en) * 2007-04-24 2010-07-22 キャリア コーポレイション Transcritical refrigerant vapor compression system with charge control
JP2011512509A (en) * 2008-02-19 2011-04-21 キャリア コーポレイション Refrigerant vapor compression system
JP2010164291A (en) * 2008-12-15 2010-07-29 Denso Corp Ejector-type refrigeration cycle
US8783060B2 (en) 2008-12-15 2014-07-22 Denso Corporation Ejector-type refrigerant cycle device
EP2312226A3 (en) * 2009-09-30 2014-10-29 Fujitsu General Limited Heat pump apparatus
US9003819B2 (en) 2009-09-30 2015-04-14 Fujitsu General Limited Heat pump apparatus using supercooling degree to control expansion valve
JP2018119741A (en) * 2017-01-25 2018-08-02 ダイキン工業株式会社 Refrigerating device

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