JPS6057163A - Refrigeration cycle - Google Patents
Refrigeration cycleInfo
- Publication number
- JPS6057163A JPS6057163A JP16496583A JP16496583A JPS6057163A JP S6057163 A JPS6057163 A JP S6057163A JP 16496583 A JP16496583 A JP 16496583A JP 16496583 A JP16496583 A JP 16496583A JP S6057163 A JPS6057163 A JP S6057163A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- refrigerant
- compressor
- pressure reducer
- refrigeration cycle
- 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
Links
Landscapes
- Saccharide Compounds (AREA)
- Fats And Perfumes (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (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】
〔発明の利用分野〕
本発明は弁制御により圧縮機停止時に冷媒の流れを11
−める冷凍サイクルにおいて、圧縮機出入1]の圧力差
を無くする冷凍サイクルに関するものである。[Detailed Description of the Invention] [Field of Application of the Invention] The present invention uses valve control to control the flow of refrigerant to 11 when the compressor is stopped.
This invention relates to a refrigeration cycle that eliminates the pressure difference between the inlet and outlet of a compressor.
〔発明の背5;1〕
従来の冷凍サイクルを第1図に示すと、1は圧縮機、2
は凝縮器、3は第1減圧器、4は第2減圧機、5は蒸発
器、6は電磁弁、7は逆止弁、8はバイパス用減圧器、
9は液−ガス分離器である。[Background of the invention 5; 1] When a conventional refrigeration cycle is shown in Fig. 1, 1 is a compressor, 2
is a condenser, 3 is a first pressure reducer, 4 is a second pressure reducer, 5 is an evaporator, 6 is a solenoid valve, 7 is a check valve, 8 is a bypass pressure reducer,
9 is a liquid-gas separator.
この様な冷凍サイクルにおいて、運転中は電磁弁6は開
き、冷媒は実線の如く流れる。この時、ガス−液分離9
で分離されたカス冷媒はバイパス用減圧器8を通って圧
縮機1に戻る。このサイクルをモリエル線図」二に画く
と第2図の実線の如くなる。圧縮機停止時は電磁弁6が
止まり、高温カスはバイパス用減圧器8を通って圧縮機
1の吸込パイプ側に戻り、圧縮機1と逆止弁7の間の■
−力を上げる。したがって、圧縮機1の停止中に、圧縮
機1の吐出側と吸込側の圧力差はなくなりバランスし起
動しやすくなる。ここで、本来なら運転中にバイパス用
減甲器8から吸込側に戻る冷媒はガス冷媒の為、性能低
下は生じない。しかし、実際には第2図において、モリ
エル線図−11のA点は飽和蒸気線上になく飽和域に入
ってしまい、性能が低下してしまうという問題が生じて
いる。これは、ガス・−液分離器か十分に働かず、ガス
が完全に分離されない為である。In such a refrigeration cycle, the solenoid valve 6 is opened during operation, and the refrigerant flows as shown by the solid line. At this time, gas-liquid separation 9
The separated refrigerant waste passes through the bypass pressure reducer 8 and returns to the compressor 1. If this cycle is plotted on a Mollier diagram, it will look like the solid line in Figure 2. When the compressor is stopped, the solenoid valve 6 is stopped, and the high-temperature waste passes through the bypass pressure reducer 8 and returns to the suction pipe side of the compressor 1.
- Increase power. Therefore, while the compressor 1 is stopped, there is no difference in pressure between the discharge side and the suction side of the compressor 1, which balances the pressure and makes it easier to start up. Here, since the refrigerant that normally returns to the suction side from the bypass armor reducer 8 during operation is a gas refrigerant, no performance deterioration occurs. However, in reality, in FIG. 2, point A of the Mollier diagram 11 is not on the saturated vapor line but falls into the saturated region, resulting in a problem that the performance deteriorates. This is because the gas-liquid separator does not work well and the gas is not completely separated.
本発明の目的は、圧縮機1の運転中に分離されtこ冷媒
に液滴が含まれても14能低下をさせない冷凍サイクル
を提供するものである。An object of the present invention is to provide a refrigeration cycle that does not cause a reduction in performance even if droplets are included in the refrigerant that is separated during operation of the compressor 1.
本発明は、減圧器により発生したガス冷媒と、減圧して
ガス−液分離器に入る冷媒と熱交換する事により、ガス
−液分離器を出た冷媒に液滴が含まれている物を蒸発器
を通さずに圧縮機吸込側にバイパスしても良くなり、理
想ナイクルが作れる。The present invention exchanges heat between the gas refrigerant generated by the pressure reducer and the refrigerant that is depressurized and enters the gas-liquid separator, thereby removing droplets from the refrigerant exiting the gas-liquid separator. It is now possible to bypass the compressor suction side without passing it through the evaporator, making it possible to create an ideal Nycle.
以下、本発明の一実施例を第3図により説明する。ガス
−液分離で分離された冷媒で、液滴を含んだ冷媒はバイ
パス用減圧器8で減圧され、低温となる。この低温冷媒
とガス−液分離器に入る冷媒とで熱交換する事により、
低温冷媒は分離器に入る冷媒を冷やす為に、第2減圧器
に入る冷媒のエンタルピを小さくし冷凍能力を増す事が
できる。An embodiment of the present invention will be described below with reference to FIG. The refrigerant separated by gas-liquid separation and containing droplets is depressurized by the bypass pressure reducer 8 and becomes low temperature. By exchanging heat between this low-temperature refrigerant and the refrigerant entering the gas-liquid separator,
Since the low-temperature refrigerant cools the refrigerant entering the separator, it is possible to reduce the enthalpy of the refrigerant entering the second pressure reducer and increase the refrigerating capacity.
これを第二2図により説明すると、運転中のモリエル線
図は点線の如くなり、圧縮機1の吸込側に入るバイパス
冷媒のエンタルピはB点となり、ガス−液分離器9から
分離された冷媒が飽和蒸気線から出たのと同じ事にする
ZJiが出来、ガス−液分部器が完全に理想的に作動し
たのと同し事となり、効率を上げる111ができる。To explain this with reference to FIG. 22, the Mollier diagram during operation becomes like a dotted line, the enthalpy of the bypass refrigerant entering the suction side of the compressor 1 is at point B, and the refrigerant separated from the gas-liquid separator 9 It is possible to create ZJi which does the same thing as if the gas had come out of the saturated steam line, and it is the same as if the gas-liquid separator operated completely ideally, and 111 to increase efficiency can be achieved.
本発明の熱交換部として、バイパス用減圧器8の出口部
と第1減圧器で熱交換器しているが、第1減圧器の代り
に、凝縮器2出11と第1減圧器の間のパイプ、又は第
1減圧器3とガス−液分離器9の間のパイプ、又はバイ
パス用減圧器8を出たパイプの代りに、バイパス用減圧
器8自体又はガス−液分離器9とバイパス用減「ε器8
の間のパイプ等と熱交換させても同等の効果を示す。As the heat exchange part of the present invention, the outlet part of the bypass pressure reducer 8 and the first pressure reducer are used as a heat exchanger. or the pipe between the first pressure reducer 3 and the gas-liquid separator 9, or the pipe leaving the bypass pressure reducer 8, the bypass pressure reducer 8 itself or the gas-liquid separator 9 and the bypass Usage “ε device 8”
The same effect can be obtained by exchanging heat with a pipe, etc. between the two.
本発明によれば、ガス−液分離器9を出た冷媒とガス−
液分離器9に入る冷媒とで熱交換させる事により、冷凍
サイクルの効率を理想サイクルにする事ができ、約4%
位の性能低下が生じてしまうのを防ぐ事ができるもので
ある。According to the present invention, the refrigerant leaving the gas-liquid separator 9 and the gas-
By exchanging heat with the refrigerant entering the liquid separator 9, the efficiency of the refrigeration cycle can be made ideal, approximately 4%.
This can prevent the performance from deteriorating as much as possible.
′第11図は従来の冷凍サイクルの説明図、第2図は本
発明を説明するモリエル線図、第3図は本発明の冷凍サ
イクルの説明図である。
■・・・圧縮機、2・・・凝縮器、3・・・第1減圧器
、4・・・第2減甲器、5・・・蒸発器、6・・・電磁
弁(ストップ弁)、7・・・逆止弁、8・・・ノくイノ
くス用減圧器、9・・・ガス−液分離器。
代理人弁理士 高 橋 明 夫' Fig. 11 is an explanatory diagram of a conventional refrigeration cycle, Fig. 2 is a Mollier diagram illustrating the present invention, and Fig. 3 is an explanatory diagram of the refrigeration cycle of the present invention. ■... Compressor, 2... Condenser, 3... First pressure reducer, 4... Second armor reducer, 5... Evaporator, 6... Solenoid valve (stop valve) , 7... Check valve, 8... Pressure reducer for NOKUINOX, 9... Gas-liquid separator. Representative Patent Attorney Akio Takahashi
Claims (1)
ー液分部1器(9)、第2減圧器(4)、ストップ弁(
6)、蒸発器(5)、逆11ユ弁(7)を連結してなる
冷凍サイクルにおいて、ガスー液分II器(9)を出た
パイプにバイパス用減圧器(8)を設けてrW H?+
機(1)と逆止弁(7)の間にバイパスし、凝縮器(2
)とガス−液分離器(9)の間の冷媒と、ガス−液分離
器(9)と圧縮機(1)の吸込側に接続するパイプとで
熱交換させた事を特徴とする冷凍サイクル。Compressor (1), condenser (2), first reducer (3), gas-liquid section 1 unit (9), second pressure reducer (4), stop valve (
6) In a refrigeration cycle in which an evaporator (5) and a reverse 11 valve (7) are connected, a bypass pressure reducer (8) is provided on the pipe exiting the gas-liquid fraction II device (9), and rW H ? +
The condenser (2) is bypassed between the machine (1) and the check valve (7).
) and a gas-liquid separator (9), and a pipe connecting the gas-liquid separator (9) and the suction side of the compressor (1) to exchange heat. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16496583A JPS6057163A (en) | 1983-09-09 | 1983-09-09 | Refrigeration cycle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16496583A JPS6057163A (en) | 1983-09-09 | 1983-09-09 | Refrigeration cycle |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6057163A true JPS6057163A (en) | 1985-04-02 |
Family
ID=15803234
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16496583A Pending JPS6057163A (en) | 1983-09-09 | 1983-09-09 | Refrigeration cycle |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6057163A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5250481A (en) * | 1991-12-28 | 1993-10-05 | Samsung Electro-Mechanics Co., Ltd. | High dielectric ceramic composition |
-
1983
- 1983-09-09 JP JP16496583A patent/JPS6057163A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5250481A (en) * | 1991-12-28 | 1993-10-05 | Samsung Electro-Mechanics Co., Ltd. | High dielectric ceramic composition |
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