JPH0330774Y2 - - Google Patents

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Publication number
JPH0330774Y2
JPH0330774Y2 JP12141284U JP12141284U JPH0330774Y2 JP H0330774 Y2 JPH0330774 Y2 JP H0330774Y2 JP 12141284 U JP12141284 U JP 12141284U JP 12141284 U JP12141284 U JP 12141284U JP H0330774 Y2 JPH0330774 Y2 JP H0330774Y2
Authority
JP
Japan
Prior art keywords
pressure
evaporation
discharge side
controller
refrigerant
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
Application number
JP12141284U
Other languages
Japanese (ja)
Other versions
JPS6138460U (en
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
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Priority to JP12141284U priority Critical patent/JPS6138460U/en
Publication of JPS6138460U publication Critical patent/JPS6138460U/en
Application granted granted Critical
Publication of JPH0330774Y2 publication Critical patent/JPH0330774Y2/ja
Granted legal-status Critical Current

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  • Air Conditioning Control Device (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Description

【考案の詳細な説明】 (産業上の利用分野) 本考案は、例えば車両や家庭等で使用される冷
凍機において、蒸発器の凍結防止機能を備えた、
冷凍サイクルにおける蒸発圧力制御装置に関する
ものである。
[Detailed description of the invention] (Industrial field of application) The present invention is a refrigerator that is used in vehicles, homes, etc., and is equipped with an evaporator antifreeze function.
The present invention relates to an evaporation pressure control device in a refrigeration cycle.

(従来の技術) 従来の、上述したような冷凍サイクルにおける
蒸発圧力制御装置は、例えば、実公昭50−40123
号公報に開示されているように、冷凍サイクルを
構成する蒸発器と圧縮機とを結ぶ配管途中に蒸発
圧力制御器を配設し、この蒸発圧力制御器の吐出
側に膨張弁の均圧管を直結した構造であつた。
(Prior Art) A conventional evaporation pressure control device for a refrigeration cycle as described above is, for example, disclosed in Japanese Utility Model Publication No. 50-40123.
As disclosed in the publication, an evaporation pressure controller is installed in the middle of the piping connecting the evaporator and compressor that make up the refrigeration cycle, and a pressure equalization pipe of the expansion valve is connected to the discharge side of the evaporation pressure controller. It was a directly connected structure.

(考案が解決しようとする課題) 斯かる従来装置にあつては、均圧管を蒸発圧力
制御器の吐出側に直結した構造であるため、低熱
負荷時に蒸発圧力制御器の吸入側圧力は、最低圧
力が2.1Kg/cm2G以上に制御される。しかし、蒸
発圧力制御器の吐出側圧力は、特に圧縮機の高速
回転時に1Kg/cm2G以下にもなつてしまい、膨張
弁は全開に近い状態となる。このため、適正量以
上の冷媒が蒸発器に流れて、リキツドバツク等に
よる悪影響を圧縮機に与えると共に、圧縮機の消
費動力が増加するという問題点があつた。
(Problem to be solved by the invention) In such a conventional device, since the pressure equalization pipe is directly connected to the discharge side of the evaporation pressure controller, the suction side pressure of the evaporation pressure controller is at the lowest level during low heat load. The pressure is controlled to 2.1Kg/cm 2 G or more. However, the discharge side pressure of the evaporation pressure controller becomes less than 1 kg/cm 2 G, especially when the compressor rotates at high speed, and the expansion valve becomes close to fully open. As a result, a problem arises in that more than the appropriate amount of refrigerant flows into the evaporator, which adversely affects the compressor due to liquid back and the like, and the power consumption of the compressor increases.

本考案は、上記事情に鑑みてなされたもので、
適正量以上の冷媒が蒸発器に流れることによるリ
キツドバツク等による悪影響を圧縮機に与えるの
を防止すると共に、圧縮機の消費電力を著しく低
減させた冷凍サイクルにおける蒸発圧力制御装置
を提供することを目的とする。
This invention was made in view of the above circumstances,
It is an object of the present invention to provide an evaporation pressure control device in a refrigeration cycle that prevents the compressor from being adversely affected by liquid back caused by more than an appropriate amount of refrigerant flowing into the evaporator, and also significantly reduces the power consumption of the compressor. shall be.

(課題を解決するための手段) 上記目的を達成するため本考案は、圧縮機で圧
縮した冷媒ガスを凝縮機で凝縮して受液器に冷媒
液として蓄え、この冷媒液を、感温筒の感知温度
と均圧管の圧力とにより弁開度が決定される膨張
弁内に流入させて断熱膨張させて霧化状態にし
て、この霧化冷媒を蒸発器で蒸発させた後、前記
蒸発器の凍結防止用の蒸発圧力制御器を介して再
び圧縮機に吸入させるようにした冷凍サイクルに
おいて、前記蒸発圧力制御器と膨張弁とを結ぶ均
圧管の取出口を、この蒸発圧力制御器の吸入側と
吐出側とにそれぞれ設けると共に、前記均圧管の
途中に、前記蒸発圧力制御器の吸入側と吐出側と
の圧力差が所定値以下のときこの蒸発圧力制御器
の吐出側圧力を前記均圧管へ伝達し且つ前記圧力
差が所定値以上のとき前記吐出側圧力より高い前
記吸入側圧力を前記均圧管に伝達する如く切換動
作する三方切換バルブを設けたことを特徴とする
ものである。
(Means for Solving the Problems) In order to achieve the above object, the present invention condenses refrigerant gas compressed by a compressor in a condenser and stores it as a refrigerant liquid in a liquid receiver, and transfers this refrigerant liquid to a thermosensor tube. The refrigerant flows into an expansion valve whose opening degree is determined by the sensed temperature of the refrigerant and the pressure of the pressure equalizing pipe, and is adiabatically expanded to form an atomized state. After evaporating this atomized refrigerant in an evaporator, In a refrigeration cycle in which suction is returned to the compressor via an evaporation pressure controller for freezing prevention, the outlet of the pressure equalization pipe connecting the evaporation pressure controller and the expansion valve is connected to the suction of the evaporation pressure controller. and a discharge side of the evaporation pressure controller, and a pressure equalizer is installed in the middle of the pressure equalization pipe to adjust the pressure on the discharge side of the evaporation pressure controller when the pressure difference between the suction side and the discharge side of the evaporation pressure controller is less than a predetermined value. The present invention is characterized in that a three-way switching valve is provided which operates to transmit the suction side pressure, which is higher than the discharge side pressure, to the pressure equalization tube when the pressure difference is above a predetermined value.

(作用) 蒸発圧力制御器の吸入側と吐出側との圧力差が
所定値以下のときは、三方切換バルブは所定状態
に切り換わつて、この蒸発圧力制御器の吐出側圧
力が均圧管へ伝達されて、クールダウン性能は従
来通りに発揮される。また、蒸発圧力制御器の吸
入側と吐出側との圧力差が所定値以上のときは、
三方切換バルブは所定状態に切り換わつて、この
蒸発圧力制御器の吐出側圧力より高い前記吸入側
圧力が均圧管へ伝達されて、膨張弁の開度は低く
なり、スーパーヒートが維持されて、リキツドバ
ツクが改善される。
(Function) When the pressure difference between the suction side and the discharge side of the evaporation pressure controller is less than a predetermined value, the three-way switching valve switches to a predetermined state, and the pressure on the discharge side of the evaporation pressure controller is transferred to the pressure equalization pipe. The cooldown performance will be carried out as before. Also, when the pressure difference between the suction side and the discharge side of the evaporation pressure controller is more than a predetermined value,
The three-way switching valve is switched to a predetermined state, and the suction side pressure, which is higher than the discharge side pressure of the evaporation pressure controller, is transmitted to the pressure equalization pipe, the opening degree of the expansion valve is lowered, and superheat is maintained. , liquid back is improved.

(実施例) 以下、本考案の一実施例を添付図面に基づいて
説明する。
(Example) Hereinafter, an example of the present invention will be described based on the accompanying drawings.

第1図は本考案に係る蒸発圧力制御装置を備え
た冷凍サイクルの構成図であり、同図中、1は凝
縮器、2は圧縮機、3は受液器、4は膨張弁、5
は蒸発器、6は、蒸発器5と圧縮機2の吐出口と
を結ぶ吐出側配管7の途中に設けられた蒸発圧力
制御器であつて、蒸発器5の蒸発圧力を制御して
この蒸発器5の凍結を防止するものである。ま
た、8は蒸発器5の吐出側配管7の温度を検出す
る感温筒であり、膨張弁4の弁開度を調節するも
のである。
FIG. 1 is a block diagram of a refrigeration cycle equipped with an evaporation pressure control device according to the present invention, in which 1 is a condenser, 2 is a compressor, 3 is a liquid receiver, 4 is an expansion valve, and 5
6 is an evaporator, and 6 is an evaporation pressure controller installed in the middle of the discharge side pipe 7 connecting the evaporator 5 and the discharge port of the compressor 2, and controls the evaporation pressure of the evaporator 5 to control the evaporation. This prevents the container 5 from freezing. Further, 8 is a temperature-sensitive tube that detects the temperature of the discharge side pipe 7 of the evaporator 5, and is used to adjust the valve opening degree of the expansion valve 4.

蒸発圧力制御器6の吸入側6a、及び吐出側6
bと、膨張弁4との間には、均圧管10が接続さ
れている。この均圧管10の途中には、蒸発圧力
制御器6の吸入側6aの圧力P1と、吐出側6b
の圧力P2との圧力差ΔPcによつて開閉し、且つそ
の圧力P1、または、P2を膨張弁4に伝達する三
方切換バルブ11が介装されている。
Suction side 6a and discharge side 6 of evaporation pressure controller 6
A pressure equalizing pipe 10 is connected between the expansion valve 4 and the expansion valve 4. In the middle of this pressure equalizing pipe 10, there is a pressure P 1 on the suction side 6a of the evaporation pressure controller 6, and a pressure P1 on the discharge side 6b.
A three-way switching valve 11 that opens and closes depending on the pressure difference ΔP c between the pressure P 2 and the pressure P 2 and transmits the pressure P 1 or P 2 to the expansion valve 4 is interposed.

三方切換バルブ11は、第2図、及び第3図に
示すように蒸発圧力制御器6の吸入側6aに接続
される吸入口11aと、吐出側6bに接続される
吐出口11bと、膨張弁4の均圧管10に接続さ
れる均圧口11cとを備えたバルブケーシング1
2内に、開口部13を備えた断面凹状のバルブ本
体14を摺動自在に嵌装してなり、このバルブ本
体14は、吐出口11b側内部に設けられたスプ
リング15により、常に吸入口11a側に付勢さ
れている。
As shown in FIGS. 2 and 3, the three-way switching valve 11 has an inlet port 11a connected to the inlet side 6a of the evaporation pressure controller 6, a discharge port 11b connected to the discharge side 6b, and an expansion valve. The valve casing 1 includes a pressure equalizing port 11c connected to the pressure equalizing pipe 10 of No. 4.
2, a valve body 14 having a concave cross section and an opening 13 is slidably fitted in the valve body 14. This valve body 14 is always connected to the suction port 11a by a spring 15 provided inside the discharge port 11b side. biased toward the side.

なお、蒸発圧力制御器6の吸入側6aの圧力
P1と、吐出側6bの圧力P2との圧力差ΔPcを所定
値、例えば0.8Kg/cm2とし、スプリング15のバ
ネ定数を0.02Kg/mm、バルブ本体14の直径を5φ
とすると、バルブ本体14の開弁時のスプリング
15の歪み長さは、π/4×0.52×0.8/0.02=8
mmとなる。
Note that the pressure on the suction side 6a of the evaporation pressure controller 6
The pressure difference ΔP c between P 1 and the pressure P 2 on the discharge side 6b is set to a predetermined value, for example, 0.8 Kg/cm 2 , the spring constant of the spring 15 is 0.02 Kg/mm, and the diameter of the valve body 14 is 5φ.
Then, the strain length of the spring 15 when the valve body 14 is opened is π/4×0.5 2 ×0.8/0.02=8
mm.

今、仮にP1−P2=1Kg/cm2のときのスプリン
グ15は、0.2Kg/cm2×π/4×0.52×0.02=2mm
圧縮されて開弁し、膨張弁4の均圧管10側のキ
ヤピラリーに蒸発圧力制御器6の吸入側6aの冷
媒が流れ込む。そのため、膨張弁4の均圧口11
cの圧力P3は、蒸発圧力制御器6の吐出側圧力
P2より高い圧力に達して、膨張弁4の弁開度が
適正開度に絞られる。
Now, if P 1 - P 2 = 1Kg/cm 2 , the spring 15 is 0.2Kg/cm 2 ×π/4×0.5 2 ×0.02 = 2mm
The refrigerant is compressed and opened, and the refrigerant on the suction side 6a of the evaporation pressure controller 6 flows into the capillary on the pressure equalization pipe 10 side of the expansion valve 4. Therefore, the pressure equalization port 11 of the expansion valve 4
The pressure P3 of c is the discharge side pressure of the evaporation pressure controller 6.
When a pressure higher than P 2 is reached, the valve opening of the expansion valve 4 is throttled to an appropriate opening.

次に、上記構成に成る本考案の蒸発圧力制御装
置の動作を説明する。
Next, the operation of the evaporation pressure control device of the present invention having the above configuration will be explained.

先ず圧縮機2で圧縮された冷媒ガスは、凝縮器
1で凝縮され、受液器3に冷媒液として蓄えられ
る。そして、感温筒8と蒸発圧力制御器6に接続
された三方切換バルブ11、及び均圧管10によ
り、膨張弁4の弁開度が決定され、膨張弁4内に
冷媒液が流入し、冷媒液は断熱膨張して霧化す
る。更に、この霧化した冷媒は、蒸発器5で蒸発
し、冷媒と熱交換した空気は冷却される。
First, the refrigerant gas compressed by the compressor 2 is condensed by the condenser 1 and stored in the receiver 3 as a refrigerant liquid. Then, the valve opening degree of the expansion valve 4 is determined by the three-way switching valve 11 and the pressure equalization pipe 10 connected to the temperature sensing tube 8 and the evaporation pressure controller 6, and the refrigerant liquid flows into the expansion valve 4. The liquid expands adiabatically and becomes atomized. Furthermore, this atomized refrigerant is evaporated in the evaporator 5, and the air that has exchanged heat with the refrigerant is cooled.

このとき、蒸発圧力制御器6によつて蒸発器5
内部の圧力が制御されて、蒸発器5のフイン及び
管壁の温度が氷点以下になつて凍結するのを防止
している。
At this time, the evaporator 5 is controlled by the evaporating pressure controller 6.
The internal pressure is controlled to prevent the temperature of the fins and tube wall of the evaporator 5 from dropping below the freezing point and freezing.

次に、三方切換バルブ11の動作を詳細に説明
する。
Next, the operation of the three-way switching valve 11 will be explained in detail.

例えば、熱負荷が高いときに、図示しないクラ
ツチをONにすると、蒸発圧力制御器6の図示し
ないパイロツトバルブ及びメインバルブは全開に
近い状態となつて、多量の冷媒が流れる。
For example, when a clutch (not shown) is turned on when the heat load is high, the pilot valve and main valve (not shown) of the evaporation pressure controller 6 are nearly fully open, allowing a large amount of refrigerant to flow.

このとき蒸発圧力制御器6の吸入側6aの圧力
P1と吐出側6bの圧力P2との圧力差ΔPcは、所定
値以下のため(P1−P2<ΔPc)、第2図に示すよ
うに吸入口11aと均圧口11cとが遮断し且つ
吐出口11bと均圧口11cとが連通した第1切
換状態に切り換わり、膨張弁4の均圧管10には
吐出側圧力P2が伝達され、クールダウン性能は
従来通り発揮される。
At this time, the pressure on the suction side 6a of the evaporation pressure controller 6
Since the pressure difference ΔP c between P 1 and the pressure P 2 on the discharge side 6b is less than a predetermined value (P 1 −P 2 <ΔP c ), as shown in FIG. is shut off and the discharge port 11b and the pressure equalization port 11c are in communication with each other, the discharge side pressure P2 is transmitted to the pressure equalization pipe 10 of the expansion valve 4, and the cool-down performance is maintained as before. Ru.

一方、低熱負荷で特に高回転時の蒸発圧力制御
器6の吸入側圧力P1は、最低圧力(2.1Kg/cm2G)
以上に保持されると共に、蒸発圧力制御器6の吐
出側圧力P2との圧力差ΔPcが、所定値以上(P1
P2>ΔPc)になると、三方切換バルブ11は、第
3図に示すように吐出口11bと均圧口11cと
が遮断し且つ吸入口11aと均圧口11cとが連
通した第2切換状態に切り換わり、均圧管10に
は、吐出側圧力P2よりも高い吸入側圧力P1が伝
達されて、膨張弁4の開度は小さくなり、スーパ
ーヒート(加熱度)が一定に維持されてリキツド
バツクが改善されるものである。
On the other hand, the suction side pressure P1 of the evaporation pressure controller 6 at low heat load and especially at high rotation is the lowest pressure (2.1Kg/cm 2 G)
At the same time, the pressure difference ΔP c with the discharge side pressure P 2 of the evaporation pressure controller 6 is maintained at a predetermined value or more (P 1
When P 2 > ΔP c ), the three-way switching valve 11 switches to the second switching mode, as shown in FIG. state, the suction side pressure P1 , which is higher than the discharge side pressure P2 , is transmitted to the pressure equalization pipe 10, the opening degree of the expansion valve 4 becomes smaller, and the superheat (heating degree) is maintained constant. Therefore, the liquid back is improved.

(考案の効果) 以上の如く本考案は、圧縮機で圧縮した冷媒ガ
スを凝縮器で凝縮して受液器に冷媒液として蓄
え、この冷媒液を、感温筒の感知温度と均圧管の
圧力とにより弁開度が決定される膨張弁内に流入
させて断熱膨張させて霧化状態にして、この霧化
冷媒を蒸発器で蒸発させた後、前記記蒸発器の凍
結防止用の蒸発圧力制御器を介して再び圧縮機に
吸入させるようにした冷凍サイクルにおいて、前
記蒸発圧力制御器と膨張弁とを結ぶ均圧管の取出
口を、この蒸発圧力制御器の吸入側と吐出側とに
それぞれ設けると共に、前記均圧管の途中に、前
記蒸発圧力制御器の吸入側と吐出側との圧力差が
所定値以下のときこの蒸発圧力制御器の吐出側圧
力を前記均圧管へ伝達し且つ前記圧力差が所定値
以上のとき前記吐出側圧力より高い前記吸入側圧
力を前記均圧管に伝達する如く切換動作する三方
切換バルブを設けたことを特徴とするものであ
る。
(Effects of the invention) As described above, the present invention condenses the refrigerant gas compressed by the compressor in the condenser and stores it in the liquid receiver as refrigerant liquid. The atomized refrigerant is allowed to flow into an expansion valve whose opening degree is determined by the pressure and is adiabatically expanded to form an atomized state, and then evaporated in an evaporator. In a refrigeration cycle in which suction is fed into the compressor again via a pressure controller, an outlet of a pressure equalizing pipe connecting the evaporation pressure controller and the expansion valve is connected to the suction side and the discharge side of the evaporation pressure controller. are provided in the middle of the pressure equalization pipe, and transmit the pressure on the discharge side of the evaporation pressure controller to the pressure equalization pipe when the pressure difference between the suction side and the discharge side of the evaporation pressure controller is less than a predetermined value; The present invention is characterized in that a three-way switching valve is provided which operates to transmit the suction side pressure higher than the discharge side pressure to the pressure equalizing pipe when the pressure difference is greater than a predetermined value.

従つて、蒸発器の吐出側の冷媒が一定の加熱度
を持つように冷媒流量を制御することができ、リ
キツドバツク等の悪影響が圧縮機に作用するのを
未然に防止できると共に、圧縮機の消費動力を著
しく低減でき、運転効率の高い冷凍サイクルを得
ることができるという効果がある。
Therefore, the refrigerant flow rate can be controlled so that the refrigerant on the discharge side of the evaporator has a constant heating degree, and it is possible to prevent adverse effects such as liquid back from acting on the compressor, and to reduce the consumption of the compressor. This has the effect that power can be significantly reduced and a refrigeration cycle with high operating efficiency can be obtained.

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

図面は本考案の一実施例を示し、第1図は本考
案に係る蒸発圧力制御装置を備えた冷凍サイクル
の構成図、第2図及び第3図は同装置における三
方切換バルブの作動説明図である。 1……凝縮器、2……圧縮機、3……受液器、
4……膨張弁、5……蒸発器、6……蒸発圧力制
御器、6a……吸入側、6b……吐出側、8……
感温筒、10……均圧管、11……三方切換バル
ブ、P1……吸入側圧力、P2……吐出側圧力、ΔPc
……圧力差、P3……均圧口の圧力。
The drawings show an embodiment of the present invention, and FIG. 1 is a block diagram of a refrigeration cycle equipped with an evaporation pressure control device according to the present invention, and FIGS. 2 and 3 are explanatory diagrams of the operation of a three-way switching valve in the device. It is. 1...Condenser, 2...Compressor, 3...Liquid receiver,
4... Expansion valve, 5... Evaporator, 6... Evaporation pressure controller, 6a... Suction side, 6b... Discharge side, 8...
Temperature sensing tube, 10...Pressure equalization pipe, 11...Three-way switching valve, P1 ...Suction side pressure, P2 ...Discharge side pressure, ΔP c
...Pressure difference, P 3 ...Pressure at pressure equalization port.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 圧縮機で圧縮した冷媒ガスを凝縮器で凝縮して
受液器に冷媒液として蓄え、この冷媒液を、感温
筒の感知温度と均圧管の圧力とにより弁開度が決
定される膨張弁内に流入させて断熱膨張させて霧
化状態にして、この霧化冷媒を蒸発器で蒸発させ
た後、前記蒸発器の凍結防止用の蒸発圧力制御器
を介して再び圧縮機に吸入させるようにした冷凍
サイクルにおいて、前記蒸発圧力制御器と膨張弁
とを結ぶ均圧管の取出口を、この蒸発圧力制御器
の吸入側と吐出側とにそれぞれ設けると共に、前
記均圧管の途中に、前記蒸発圧力制御器の吸入側
と吐出側との圧力差が所定値以下のときこの蒸発
圧力制御器の吐出側圧力を前記均圧管へ伝達し且
つ前記圧力差が所定値以上のとき前記吐出側圧力
より高い前記吸入側圧力を前記均圧管に伝達する
如く切換動作する三方切換バルブを設けたことを
特徴とする冷凍サイクルにおける蒸発圧力制御装
置。
Refrigerant gas compressed by a compressor is condensed in a condenser and stored as refrigerant liquid in a liquid receiver, and this refrigerant liquid is transferred to an expansion valve whose valve opening degree is determined by the sensed temperature of a temperature-sensitive cylinder and the pressure of a pressure equalization pipe. After the atomized refrigerant is evaporated in an evaporator, it is sucked into the compressor again via an evaporation pressure controller for freezing prevention of the evaporator. In the refrigeration cycle, an outlet of the pressure equalization pipe connecting the evaporation pressure controller and the expansion valve is provided on the suction side and the discharge side of the evaporation pressure controller, respectively. When the pressure difference between the suction side and the discharge side of the pressure controller is less than a predetermined value, the discharge side pressure of this evaporation pressure controller is transmitted to the pressure equalization pipe, and when the pressure difference is more than a predetermined value, the discharge side pressure is transmitted to the pressure equalization pipe. An evaporation pressure control device for a refrigeration cycle, comprising a three-way switching valve that operates to transmit the high suction side pressure to the pressure equalization pipe.
JP12141284U 1984-08-09 1984-08-09 Evaporation pressure control device in refrigeration cycle Granted JPS6138460U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12141284U JPS6138460U (en) 1984-08-09 1984-08-09 Evaporation pressure control device in refrigeration cycle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12141284U JPS6138460U (en) 1984-08-09 1984-08-09 Evaporation pressure control device in refrigeration cycle

Publications (2)

Publication Number Publication Date
JPS6138460U JPS6138460U (en) 1986-03-11
JPH0330774Y2 true JPH0330774Y2 (en) 1991-06-28

Family

ID=30680198

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12141284U Granted JPS6138460U (en) 1984-08-09 1984-08-09 Evaporation pressure control device in refrigeration cycle

Country Status (1)

Country Link
JP (1) JPS6138460U (en)

Also Published As

Publication number Publication date
JPS6138460U (en) 1986-03-11

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