JPS60200054A - Refrigerator - Google Patents

Refrigerator

Info

Publication number
JPS60200054A
JPS60200054A JP5666784A JP5666784A JPS60200054A JP S60200054 A JPS60200054 A JP S60200054A JP 5666784 A JP5666784 A JP 5666784A JP 5666784 A JP5666784 A JP 5666784A JP S60200054 A JPS60200054 A JP S60200054A
Authority
JP
Japan
Prior art keywords
evaporator
refrigerant
check valve
rotary compressor
temperature
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
JP5666784A
Other languages
Japanese (ja)
Inventor
藤本 眞嗣
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
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 Matsushita Refrigeration Co filed Critical Matsushita Refrigeration Co
Priority to JP5666784A priority Critical patent/JPS60200054A/en
Publication of JPS60200054A publication Critical patent/JPS60200054A/en
Pending legal-status Critical Current

Links

Landscapes

  • Devices That Are Associated With Refrigeration Equipment (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、逆止弁を有するロータリーコンプレッサを用
いた冷凍装置に関し、特にその圧損低減に係わる。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a refrigeration system using a rotary compressor having a check valve, and particularly relates to reducing pressure loss thereof.

従来例の構成とその問題点 従来の冷凍・冷蔵庫に使用する冷凍装置は第1図に示す
様に、ロータリーコンプレ、フサ1.コンデンサ2.キ
ヤピラリチユーブ3.エバポレータ4を順次接続して冷
却システムを形成している。
Structure of the conventional example and its problems As shown in Fig. 1, the refrigeration equipment used in the conventional freezer/refrigerator consists of a rotary compressor, a casing 1. Capacitor 2. Capillary tube 3. The evaporators 4 are connected in sequence to form a cooling system.

5はロータリーコンプレッサ1の運転停止に同期して開
閉する開閉弁で、ロータリーコンプレ291が停止した
ときコンデンサ2内の高圧高温冷媒がキャピラリチュー
ブ3を通じて低圧低温のエノくポレータ4内に流入し、
エバポレータ4の熱負荷となるのを防止するものである
。6は逆止弁でロータリーコンプレッサ1が停止したと
き、ロータリーコンプレッサ1内が高圧高温ガス冷媒が
、機械室7より流出し、吸入管8を逆流して低圧低温の
エバポレータ4内に流入し熱負荷となるのを防止するも
のである。逆止弁6は、ボール弁9とボール弁9の移動
を阻止する網目状のストツ/′ニー10と弁座11とよ
り成り、ケーシング12にストッパー10と弁座11を
一体固定して形成している。
5 is an on-off valve that opens and closes in synchronization with the stoppage of the rotary compressor 1, and when the rotary compressor 291 stops, the high-pressure, high-temperature refrigerant in the condenser 2 flows through the capillary tube 3 into the low-pressure, low-temperature enochorator 4;
This prevents the evaporator 4 from becoming a heat load. 6 is a check valve, and when the rotary compressor 1 stops, the high-pressure, high-temperature gas refrigerant inside the rotary compressor 1 flows out from the machine room 7, flows backward through the suction pipe 8, and flows into the low-pressure, low-temperature evaporator 4, causing a heat load. This is to prevent this from happening. The check valve 6 is composed of a ball valve 9, a mesh-like stop/knee 10 for preventing movement of the ball valve 9, and a valve seat 11, and is formed by integrally fixing the stopper 10 and the valve seat 11 to a casing 12. ing.

弁座11にはボール弁9の径より小さい径を有する冷媒
通路13が設けられている。吸入管8はキャピラリチュ
ーブ′3と熱交換し、キャピラリチューブ3内の冷媒の
過冷却を促進し、冷凍サイクルの冷凍効果を大きくする
様にしている。
A refrigerant passage 13 having a smaller diameter than the diameter of the ball valve 9 is provided in the valve seat 11 . The suction pipe 8 exchanges heat with the capillary tube '3, promotes supercooling of the refrigerant in the capillary tube 3, and increases the refrigeration effect of the refrigeration cycle.

上記構成において、ロータリーコンプレッサ1の停止中
は、開閉弁5が閉路され、逆止弁6もロータリーコンプ
レッサ1の機構部7からの冷媒逆流によりボール弁9は
第1図の点線9′の様に弁座11に押付けられることに
より閉路されておシ、ロータリーコンプレッサ、コンデ
ンサ益内の高圧高温冷媒が、エバポレータ4に’流入す
るのを防止する。又、ロータリーコンプレッサ1が運転
中は、開閉弁6は開路され、逆止弁6もボール弁9が冷
媒流により第1図の実線 に示す様にストッパー10に
押し伺けられ開路されておシ、冷媒はロータリーコンプ
レッサ1.コンデンサ2.キャピラリチューブ3.エバ
ポレータ4.吸入管8と流れ、吸入管8中でキャピラリ
チューブ3と熱交換した後、比較的高い温度の比較体積
の大きいガス冷媒となって逆止弁6の冷媒通路13に流
れた後、ロータリーコンプレッサ1に吸込まれ正常な冷
却運転を行なう。逆止弁6の弁座11に設けられた冷媒
通路13は出来るだけ小さい方がボール弁7が閉路した
ときの洩れ量が少なくできるが、逆にロータリーコンプ
レッザ運転中は冷媒通路13により大きな圧損が生じロ
ータリーコンプレッサ1の吸入圧力が低減し、性能が低
下する欠点がある。
In the above configuration, when the rotary compressor 1 is stopped, the on-off valve 5 is closed, and the check valve 6 is also caused by the backflow of refrigerant from the mechanical part 7 of the rotary compressor 1. The circuit is closed by being pressed against the valve seat 11 to prevent high pressure and high temperature refrigerant in the rotary compressor and condenser from flowing into the evaporator 4. Furthermore, while the rotary compressor 1 is in operation, the on-off valve 6 is opened, and the check valve 6 is also opened as the ball valve 9 is pushed by the stopper 10 due to the refrigerant flow as shown by the solid line in Fig. 1. , the refrigerant is a rotary compressor 1. Capacitor 2. Capillary tube 3. Evaporator 4. After flowing into the suction pipe 8 and exchanging heat with the capillary tube 3 in the suction pipe 8, it becomes a gas refrigerant with a relatively high temperature and a relatively large volume, and flows into the refrigerant passage 13 of the check valve 6, and then flows into the rotary compressor 1. Normal cooling operation is performed. The smaller the refrigerant passage 13 provided in the valve seat 11 of the check valve 6, the smaller the amount of leakage when the ball valve 7 is closed, but on the other hand, during rotary compressor operation, the refrigerant passage 13 causes a large pressure drop. This has the disadvantage that the suction pressure of the rotary compressor 1 is reduced and the performance is degraded.

又、吸入管8とキャピラリNチューブ3を熱交換するこ
とにより、キャピラリNチューブ3内の冷媒の過冷却を
促進させ冷凍サイクルの冷凍効果を増大させているが、
反面吸入管8内のガス冷媒温度が上昇し、比較的温度の
高い比体積の大きい過熱ガスとなって吸入管8と逆止弁
6内を流れる為、吸入管8と逆止弁6内の冷媒通路13
で生じる圧損が非常に大きくなるという欠点を有してい
た。
Furthermore, by exchanging heat between the suction pipe 8 and the capillary N tube 3, supercooling of the refrigerant in the capillary N tube 3 is promoted and the refrigeration effect of the refrigeration cycle is increased.
On the other hand, the temperature of the gas refrigerant in the suction pipe 8 rises, turning into superheated gas with a relatively high temperature and large specific volume, which flows through the suction pipe 8 and the check valve 6. Refrigerant passage 13
The disadvantage was that the pressure loss caused by this process was extremely large.

発明の目的 そこで本発明は、吸入管及び逆止弁を流れるガス冷媒量
を減少すると共に冷媒の温度を下げ吸入管及び逆止弁で
生じる圧損を低減すると共に、ロータリーコンプレッサ
の吸入ガス温度を低減することを目的とする。
Purpose of the Invention Therefore, the present invention reduces the amount of gas refrigerant flowing through the suction pipe and the check valve, lowers the temperature of the refrigerant, reduces the pressure loss occurring in the suction pipe and the check valve, and reduces the temperature of the intake gas of the rotary compressor. The purpose is to

発明の構成 この目的を達成する為、本発明は、エバポレータを2分
割し、第1のエバポレータと第2のエフ5ポレータ間よ
シ、第2エバポレータと逆止弁をバイパスするバイパス
回路を設け、前記バイパス回路をキャピラリチューブ及
びコンデンサの一部と熱交換し、且つ前記バイパス回路
の熱交換部より下流側に逆上弁機構付放熱器を設けるこ
とによりロータリーコンプレッサ停止中のエバポレータ
の冷媒流入を防止するとともに吸入管と逆止弁を通過す
る冷媒量を低減させるだけでなく、冷媒温度も低減させ
るととにより、第2のエバポレータ吸入管、逆止弁で生
じる圧損を低減させるものである。又、キャピラリチュ
ーブ内の冷媒の過冷却を促進した後の高温冷媒を放熱器
にて放熱することによりコンプレッサの吸入温度を低減
するものである。
Structure of the Invention In order to achieve this object, the present invention divides the evaporator into two, and provides a bypass circuit between the first evaporator and the second evaporator and bypassing the second evaporator and the check valve. By exchanging heat with the capillary tube and part of the condenser in the bypass circuit, and by providing a radiator with a reverse valve mechanism downstream from the heat exchange section of the bypass circuit, refrigerant is prevented from flowing into the evaporator when the rotary compressor is stopped. At the same time, it not only reduces the amount of refrigerant passing through the suction pipe and check valve, but also reduces the temperature of the refrigerant, thereby reducing the pressure loss occurring in the second evaporator suction pipe and check valve. Furthermore, the suction temperature of the compressor is reduced by radiating heat from the high-temperature refrigerant in the radiator after promoting supercooling of the refrigerant in the capillary tube.

実施例の説明 以下本発明の一実施例を添付図面に従い説明するが、従
来と同一構成については同一符号を符してその詳細な説
明は省略する。第2図においてロータリーコンプレッサ
1.コンデンサ2.キャピラリチューブ3.第1のエバ
ポレータ4a、第2のエバポレータ4bを順次接続して
冷却システムを形成している。6はロータリーコンプレ
ッサ1の運転停止に同期して開閉する開閉弁で、コンデ
ンサ2の出口部に設けている。6は逆止弁で吸入管8に
設けている。14は気液分離器で、第1エバポレータ4
aと第2エバポレータ4b間に設けている。16は第1
エバポレータ4aより流出してきた冷媒のうちガス冷媒
を流すバイパス回路で入口部IE5aを気液分離器14
に、出口部16bをロータリーコンプレッサ1の入口バ
イブ16に接続している。そしてバイパス回路は、一点
鎖線部で示す様に、A部で第1のエバポレータと熱交換
した後、B部でキャピラリチューブ3とコンデンサ2の
出口バイブ2′と熱交換させている。17は逆止弁機構
付放熱器で、前記熱交換部と入口パイブ16間に設けて
いる。逆止弁機構付放熱器17は、ボール弁18とボー
ル弁18の移動を阻止する網目状のストッパー19と弁
座20と放熱フィン21を有するケーシング22とよシ
成り、ケーシング22にストッパー19と弁座20を一
体固定して形成している。弁座2oにはボール弁18の
径よシ小さい径の冷媒通路23が設けられている。バイ
パス回路15は、所定のガス冷媒が流れる様に比較的小
径のパイプで形成されており、第2エバポレータ4bと
吸入管8と逆止弁6の管抵抗より大きい抵抗になる様に
している。又第2エバポレータ4bと入口バイブ16間
の吸入管8及び逆止弁6は断熱材(0部)で断熱し、吸
入管8内の冷媒の温度が上昇するのを防止している。
DESCRIPTION OF THE EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings, but the same components as those of the prior art will be denoted by the same reference numerals and detailed explanations thereof will be omitted. In FIG. 2, rotary compressor 1. Capacitor 2. Capillary tube 3. A cooling system is formed by sequentially connecting a first evaporator 4a and a second evaporator 4b. Reference numeral 6 denotes an on-off valve that opens and closes in synchronization with the stoppage of the rotary compressor 1, and is provided at the outlet of the condenser 2. 6 is a check valve provided in the suction pipe 8. 14 is a gas-liquid separator, and the first evaporator 4
a and the second evaporator 4b. 16 is the first
The inlet part IE5a is connected to the gas-liquid separator 14 in a bypass circuit through which gas refrigerant flows out of the refrigerant flowing out from the evaporator 4a.
In addition, the outlet section 16b is connected to the inlet vibrator 16 of the rotary compressor 1. The bypass circuit exchanges heat with the first evaporator in a section A, and then exchanges heat with the capillary tube 3 and the outlet vibe 2' of the condenser 2 in a section B, as shown by the dashed line. Reference numeral 17 denotes a radiator with a check valve mechanism, which is provided between the heat exchange section and the inlet pipe 16. The radiator 17 with a check valve mechanism includes a ball valve 18 , a mesh-like stopper 19 for preventing movement of the ball valve 18 , a valve seat 20 , and a casing 22 having heat radiation fins 21 . The valve seat 20 is integrally fixed. A refrigerant passage 23 having a diameter smaller than that of the ball valve 18 is provided in the valve seat 2o. The bypass circuit 15 is formed of a relatively small diameter pipe so that a predetermined gas refrigerant flows therethrough, and is designed to have a resistance greater than the pipe resistance of the second evaporator 4b, suction pipe 8, and check valve 6. Further, the suction pipe 8 and check valve 6 between the second evaporator 4b and the inlet vibrator 16 are insulated with a heat insulating material (0 parts) to prevent the temperature of the refrigerant in the suction pipe 8 from rising.

上記構成において、ロータリーコンプレッサ1の運転中
は、開閉弁5が開路され、逆止弁6もボール弁9が冷媒
流により第2図の点線で示す様にストッパー10に押付
けられることにより開略されている。ロータリーコンプ
レッサ1から1仕出された冷媒はコンデンサ2.キヤピ
ラリチユーブ3゜第1エバポレータ4aと流れ気液分離
器14に入る。気液分離器14に入った冷媒は、気液に
分離され、液冷媒は第2エバポレータ4bに流れ、蒸発
して低温のガス冷媒となって吸入管8.逆止弁6を流れ
、入口バイブ16に入る。又ガス冷媒はバイパス回路1
5を流れ、第1エバポレータ48部にて完全に液冷媒を
蒸発させ100%の低温ガス冷媒となってキャピラリチ
ューブ3との熱交換部13に入る。低温ガス冷媒は熱交
換部Bでキャピラリチューブ3内の冷媒の過冷却を促進
させた後、コンデンサ2の出口バイブ2′と熱交換して
、高温のガス冷媒となって逆止弁機構付放熱器17に入
る。17に入った冷媒は冷媒流により、逆止弁18をス
トッパー19に押付けることにより開略し、放熱冷却さ
れ、外気温度に近い温度のガス冷媒となって入口バイブ
16に流入する。入口バイブ16で吸入管8より流入し
てきた低温ガス冷媒と、バイパス回路16の逆止弁機構
付放熱器17で放熱冷却されたガス冷媒は入口バイブ1
6内でフ褐合され比較的温度の低いガス冷媒となってロ
ータリーコンプレッサ1に吸入される。従って吸入管8
.逆止弁6を流れる冷媒流量は従来より少なくでき且つ
温度も加熱されないので第3図に示す様にaからbに低
下することができ、比体積は従来のCからdへ小さくで
きる。従って吸入管8゜逆止弁6を流れる冷媒流速は、
比体積がJ\さくなることにより、第4図に示す様に従
来のeがらfへと減少し、吸入管8.逆止弁6で生じる
圧損も従来の9からhへと大幅に減少できる。又、バイ
パス回路15を流れる冷媒は、キャピラリチューブ3で
熱交換してキャピラリチューブ3内の冷媒を過冷却する
ので従来と同様の冷凍効果の増大が得られる。そしてそ
の後逆止弁機構付放熱器17部にて放熱冷却された後入
ロバイブ16に入り、吸入管8より流れてきた低温ガス
冷媒と混合されるので、従来よジロータリーコンプレy
す1への吸入ガス温度を低減でき、ロータリーコンプレ
ッサ1を効率よく運転することができる。次にロータリ
ーコンプレッサ1が停止すると開閉弁6は閉路される。
In the above configuration, when the rotary compressor 1 is in operation, the on-off valve 5 is opened, and the check valve 6 is also opened by pressing the ball valve 9 against the stopper 10 as shown by the dotted line in FIG. 2 due to the refrigerant flow. ing. The refrigerant discharged from the rotary compressor 1 is transferred to the condenser 2. Capillary tube 3° flows into first evaporator 4a and gas-liquid separator 14. The refrigerant that has entered the gas-liquid separator 14 is separated into gas and liquid, and the liquid refrigerant flows to the second evaporator 4b, where it evaporates and becomes a low-temperature gas refrigerant that is passed through the suction pipe 8. It flows through the check valve 6 and enters the inlet vibe 16. Also, gas refrigerant uses bypass circuit 1.
5, the liquid refrigerant is completely evaporated in the first evaporator 48 section, becomes 100% low-temperature gas refrigerant, and enters the heat exchange section 13 with the capillary tube 3. The low-temperature gas refrigerant promotes supercooling of the refrigerant in the capillary tube 3 in the heat exchange section B, and then exchanges heat with the outlet vibe 2' of the condenser 2, becoming a high-temperature gas refrigerant and dissipating the heat with a check valve mechanism. Enter vessel 17. The refrigerant that has entered 17 is opened by pressing the check valve 18 against the stopper 19 due to the refrigerant flow, is cooled by heat radiation, and flows into the inlet vibe 16 as a gas refrigerant having a temperature close to the outside air temperature. The low-temperature gas refrigerant flowing in from the suction pipe 8 at the inlet vibrator 16 and the gas refrigerant heat-radiated and cooled by the radiator 17 with a check valve mechanism in the bypass circuit 16 are transferred to the inlet vibrator 1.
In the rotary compressor 1, the refrigerant is fluorinated and becomes a relatively low temperature gas refrigerant. Therefore, suction pipe 8
.. Since the flow rate of the refrigerant flowing through the check valve 6 can be lower than in the conventional case and the temperature is not heated, it can be reduced from a to b as shown in FIG. 3, and the specific volume can be reduced from the conventional C to d. Therefore, the flow rate of refrigerant flowing through the suction pipe 8° check valve 6 is:
As the specific volume J\ decreases, the conventional e decreases to f as shown in Fig. 4, and the suction pipe 8. The pressure loss caused by the check valve 6 can also be significantly reduced from the conventional 9 to h. Further, the refrigerant flowing through the bypass circuit 15 exchanges heat with the capillary tube 3 to supercool the refrigerant in the capillary tube 3, so that the same increase in the refrigerating effect as in the conventional case can be obtained. Thereafter, it enters the post-inlet pipe 16 which has been cooled by heat radiation in the radiator 17 with a check valve mechanism, and is mixed with the low-temperature gas refrigerant flowing from the suction pipe 8.
The temperature of the intake gas to the compressor 1 can be reduced, and the rotary compressor 1 can be operated efficiently. Next, when the rotary compressor 1 stops, the on-off valve 6 is closed.

そして逆止弁6もロータリーコンプレッサ1の機械部7
からの冷媒逆流によりボール弁は第2図の点線9′の様
に押付けられることにより閉路される。又逆止弁機構付
放熱器17内のボール弁19も同様に第2図の点線18
′に示す様に弁座20に押付けられることにより閉路さ
れるので従来と同様にロータリーコンプレッサ1.コン
デンサ2内の高圧高温冷媒がエバポレータ4a 4bに
流入し熱負荷となるのを防止することができる。
The check valve 6 is also the mechanical part 7 of the rotary compressor 1.
The ball valve is closed by being pushed as shown by the dotted line 9' in FIG. 2 due to the backflow of refrigerant from the ball valve. Similarly, the ball valve 19 in the radiator 17 with a check valve mechanism is also connected to the dotted line 18 in FIG.
As shown in FIG. 1, the circuit is closed by being pressed against the valve seat 20, so the rotary compressor 1. It is possible to prevent the high-pressure high-temperature refrigerant in the condenser 2 from flowing into the evaporators 4a and 4b and causing a heat load.

従って、吸入管8と逆止弁6の冷媒通路を広げることな
く、吸入管8と逆止弁6の圧損を減少することができる
と共に、ロータリーコンプレッサ1への吸入ガス温度も
低下でき、且っロータIJ−コンフレノザ1停止時にエ
バポL/−夕4a、4bへ高圧高温冷媒が流入するのも
防止できるので効率の良い冷凍装置を得ることが出来る
Therefore, the pressure drop between the suction pipe 8 and the check valve 6 can be reduced without widening the refrigerant passage between the suction pipe 8 and the check valve 6, and the temperature of the suction gas to the rotary compressor 1 can also be lowered. Since it is possible to prevent high-pressure high-temperature refrigerant from flowing into the evaporator ports 4a and 4b when the rotor IJ-confrenozer 1 is stopped, a highly efficient refrigeration system can be obtained.

発明の効果 以上の説明からも明らかなように、本発明は第1のエバ
ポレータと第2のエバポレータの上流側にロータリーコ
ンプレッサの運転停止に同期して開閉する開閉弁を、第
2エバポレータの下流側に逆止弁を、第1エバポレータ
と第2エバポレータ間より、第2エバポレータと前記逆
止弁をバイパスするバイパス回路を設け、バイパス回路
をキャピラリチューブ及びコンデンサの一部と熱交換し
、前記バイパス回路の熱交換部より下流側に逆止弁機構
付放熱器を設けたものであるから、吸入管と逆止弁の冷
媒通路を広げることなく、吸入管と逆止弁の圧損を減少
することができると共に、ロータリーコンプレッサへの
吸入ガス温度も低下でき、且つロータリーコンプレッサ
停止時にエバポレータへロータリーコンプレッサとコン
デンサの高圧高温冷媒が流入するのも防止できるので効
率の良い冷凍装置を得ることができる。
Effects of the Invention As is clear from the above explanation, the present invention provides an on-off valve that opens and closes in synchronization with the stoppage of the rotary compressor on the upstream side of the first evaporator and the second evaporator, and on the downstream side of the second evaporator. A check valve is provided between the first evaporator and the second evaporator, and a bypass circuit is provided between the first evaporator and the second evaporator to bypass the second evaporator and the check valve. Since a radiator with a check valve mechanism is installed downstream of the heat exchange section, pressure loss between the suction pipe and the check valve can be reduced without widening the refrigerant passage between the suction pipe and the check valve. At the same time, the temperature of the intake gas to the rotary compressor can be lowered, and the high-pressure, high-temperature refrigerant from the rotary compressor and condenser can be prevented from flowing into the evaporator when the rotary compressor is stopped, making it possible to obtain a highly efficient refrigeration system.

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

第1図は従来の冷凍装置の冷媒回路図、第2図は本発明
の一実施例を示す冷凍装置の冷媒回路図、第3図は従来
例及び本発明における圧力一定時の過熱ガス冷媒の温度
と比体積の関係を示す特性図、第4図は同じく吸入パイ
プと逆止弁内の流速と圧悼、の関係を示す特性図である
。 1・・・・・・ロータリーコンプレッサ、2・旧・・コ
ンデンサ、3・・・・・・キャピラリチューブ、4a・
・印・第1エバポレータ、4b・・・・・・第2エバポ
レータ、6・・・・・・逆止弁、16・・・・・・バイ
パス回路、17・・川・逆止弁機構付放熱器。 代理人の氏名 弁理士 中 尾 敏 男 はが1名第1
図 第2図
Fig. 1 is a refrigerant circuit diagram of a conventional refrigeration system, Fig. 2 is a refrigerant circuit diagram of a refrigeration system showing an embodiment of the present invention, and Fig. 3 is a diagram of a superheated gas refrigerant at constant pressure in the conventional example and the present invention. FIG. 4 is a characteristic diagram showing the relationship between temperature and specific volume, and FIG. 4 is a characteristic diagram showing the relationship between flow velocity and pressure inside the suction pipe and check valve. 1... Rotary compressor, 2... Old capacitor, 3... Capillary tube, 4a...
・Mark: 1st evaporator, 4b: 2nd evaporator, 6: Check valve, 16: Bypass circuit, 17: Heat dissipation with check valve mechanism vessel. Name of agent: Patent attorney Toshio Nakao (1st person)
Figure 2

Claims (1)

【特許請求の範囲】[Claims] (1) ロータリーコンプレッサ、コンデンサ、キャピ
ラリチューブ、第1のエバポレータ、第2のエバポレー
タを順次直列に接続して冷却システムを形成し、第1の
エバポレータの上流側に前記ロータリーコンプレッサの
運転停止に同期して開閉する開閉部を、第2エバポレー
タの下流側に逆止弁を、第1エバポレータと第2エバポ
レータ間より、第2エバポレータと前記逆止弁をバイパ
スするバイパス回路を設け、バイパス回路をキャピラリ
チューブ及びコンデンサの一部と熱交換し、前記バイパ
ス回路の熱交換部より下流側に、逆止弁機構付放熱器を
設けてなる冷凍装置。
(1) A rotary compressor, a condenser, a capillary tube, a first evaporator, and a second evaporator are connected in series to form a cooling system, and a cooling system is formed upstream of the first evaporator in synchronization with the stoppage of the rotary compressor. A check valve is provided on the downstream side of the second evaporator, a bypass circuit is provided between the first evaporator and the second evaporator to bypass the second evaporator and the check valve, and the bypass circuit is connected to a capillary tube. and a radiator with a check valve mechanism, which exchanges heat with a part of the condenser and is provided downstream of the heat exchange section of the bypass circuit.
JP5666784A 1984-03-23 1984-03-23 Refrigerator Pending JPS60200054A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5666784A JPS60200054A (en) 1984-03-23 1984-03-23 Refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5666784A JPS60200054A (en) 1984-03-23 1984-03-23 Refrigerator

Publications (1)

Publication Number Publication Date
JPS60200054A true JPS60200054A (en) 1985-10-09

Family

ID=13033756

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5666784A Pending JPS60200054A (en) 1984-03-23 1984-03-23 Refrigerator

Country Status (1)

Country Link
JP (1) JPS60200054A (en)

Similar Documents

Publication Publication Date Title
US4173865A (en) Auxiliary coil arrangement
CN101688695B (en) CO2 refrigerant system with booster circuit
JPH09170832A (en) Refrigeration cycle device with two evaporation temperatures
JPS6269066A (en) Refrigeration cycle device
JPH1019418A (en) Freezer refrigerator
JPH10325630A (en) Air conditioner
JP7603229B2 (en) Air Conditioning Equipment
JP2000292016A (en) Refrigerating cycle
JPS60200054A (en) Refrigerator
JPH08327181A (en) Heat exchanger and freezer with heat exchanger
JPS60235960A (en) Refrigerator
CN216448413U (en) Refrigerating system capable of reducing oil return temperature of compressor
JPS5818061A (en) Refrigerator
JPS60200053A (en) Refrigerator
JPH04268165A (en) Two-stage compression refrigeration cycle equipment
JPS5815819Y2 (en) air conditioner
JPH11325617A (en) Compression refrigerator
JPS6284260A (en) heating device
JPS6124950A (en) dual refrigeration equipment
SU557238A1 (en) Mtkro-cryogenic refrigerator
JPH01312365A (en) Air conditioning equipment
JPS59153074A (en) Refrigeration cycle equipment
JPH08178451A (en) Air conditioner
JPS5833068A (en) Two-stage compression refrigerating cycle
JPH0894192A (en) Vapor compression type refrigerating device