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JPS6056980B2 - refrigeration cycle - Google Patents
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JPS6056980B2 - refrigeration cycle - Google Patents

refrigeration cycle

Info

Publication number
JPS6056980B2
JPS6056980B2 JP14363779A JP14363779A JPS6056980B2 JP S6056980 B2 JPS6056980 B2 JP S6056980B2 JP 14363779 A JP14363779 A JP 14363779A JP 14363779 A JP14363779 A JP 14363779A JP S6056980 B2 JPS6056980 B2 JP S6056980B2
Authority
JP
Japan
Prior art keywords
refrigerant
compressor
gas
heat exchanger
evaporator
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
JP14363779A
Other languages
Japanese (ja)
Other versions
JPS5668754A (en
Inventor
精一 飯田
興二 竹下
豊 小澤
善一 吉田
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP14363779A priority Critical patent/JPS6056980B2/en
Publication of JPS5668754A publication Critical patent/JPS5668754A/en
Publication of JPS6056980B2 publication Critical patent/JPS6056980B2/en
Expired legal-status Critical Current

Links

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Description

【発明の詳細な説明】 本発明は空気調和機、冷凍装置等の冷凍サイクルに関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a refrigeration cycle for an air conditioner, a refrigeration device, etc.

第1図は従来の空気調和機の冷媒系統図で、1は圧縮機
、2はコンデンサ、3は膨張弁、4はエバポレータ、5
は圧縮機駆動用原動機、6はコンデンサ2の中間ポート
、7は熱交換器、8は弁、9は絞り、10は合流点であ
る。
Figure 1 is a refrigerant system diagram of a conventional air conditioner, where 1 is a compressor, 2 is a condenser, 3 is an expansion valve, 4 is an evaporator, and 5 is a refrigerant system diagram.
1 is a prime mover for driving the compressor, 6 is an intermediate port of the condenser 2, 7 is a heat exchanger, 8 is a valve, 9 is a throttle, and 10 is a confluence point.

通常運転時は、冷媒は圧縮機1、コンデンサ2、膨張弁
3、エバポレータ4、圧縮機1をこの順に流れる。室内
温度が低下したため冷房能力を下げたいとき即ち容量制
御するときは、コンデンサ2の中間ポート6より冷媒の
一部をバイパスさせ熱交換器7の1次側、弁8、絞り9
、熱交換器7の2次側を経て合流点10でエバポレータ
4からの冷媒と合流させ圧縮機1に戻す。このとき、コ
ンデンサ2を通り膨張弁3を通つてエバポレータ4へ流
れる冷媒量が少なくなり、エバポレータ4の冷房能力が
小さくなる。
During normal operation, refrigerant flows through the compressor 1, condenser 2, expansion valve 3, evaporator 4, and compressor 1 in this order. When it is desired to reduce the cooling capacity due to a drop in the indoor temperature, that is, when controlling the capacity, a part of the refrigerant is bypassed from the intermediate port 6 of the condenser 2, and the air is transferred to the primary side of the heat exchanger 7, the valve 8, and the throttle 9.
, the refrigerant passes through the secondary side of the heat exchanger 7 , joins with the refrigerant from the evaporator 4 at the merging point 10 , and returns to the compressor 1 . At this time, the amount of refrigerant flowing through the condenser 2 and the expansion valve 3 to the evaporator 4 decreases, and the cooling capacity of the evaporator 4 decreases.

上記従来装置においては、室温の如何によつては、熱交
換器7の2次側を出た冷媒は気液混合状”態となり、ま
た、室温が低く冷房負荷が小さい場合はエバポレータ4
を流れる冷媒は加熱度の低い気体となる。
In the conventional device described above, depending on the room temperature, the refrigerant leaving the secondary side of the heat exchanger 7 will be in a gas-liquid mixed state, and if the room temperature is low and the cooling load is small, the evaporator 4
The refrigerant flowing through becomes a gas with a low degree of heating.

従つて、合流点10で混合した冷媒は気液混合状態とな
ることもあり、この冷媒を圧縮機1が吸込むとその内部
で液圧縮を生じ、これ・が圧縮機1の損傷の原因となる
。このため、限られた運転条件でしか容量制御ができな
かつた。本発明は上記に鑑み容量制御時の圧縮機内部で
の液圧縮を防止し、容量制御を広範囲に、かつ、なめら
かに行なうことができるようにしたものでjあつて、以
下第2図に示す本発明の1実施例について具体的に説明
する。第2図において符号1ないし10は第1図のそれ
と同じてある。
Therefore, the refrigerant mixed at the confluence point 10 may become a gas-liquid mixture, and when this refrigerant is sucked into the compressor 1, liquid compression occurs inside the compressor 1, which can cause damage to the compressor 1. . For this reason, capacity control was only possible under limited operating conditions. In view of the above, the present invention prevents liquid compression inside the compressor during capacity control, and enables capacity control to be performed over a wide range and smoothly. One embodiment of the present invention will be specifically described. In FIG. 2, numerals 1 to 10 are the same as those in FIG.

101は熱交換器7の2次側より出た冷媒を気液分離す
るための気液分離器、102は気液分離された液冷媒を
エバポレータ4へ流すための絞り、103は気液分離さ
れたガス冷媒を圧縮機1へ流すため絞りてある。
101 is a gas-liquid separator for separating the refrigerant from the secondary side of the heat exchanger 7, 102 is a throttle for flowing the separated liquid refrigerant to the evaporator 4, and 103 is a gas-liquid separated refrigerant. The gas refrigerant is throttled to flow into the compressor 1.

コンデンサ2の中間ボート6より抽出された冷媒は、熱
交換器7の1次側、弁8、絞り9を通り、再び熱交換器
7の2次側に戻り、次いで気液分離器101に入る。
The refrigerant extracted from the intermediate boat 6 of the condenser 2 passes through the primary side of the heat exchanger 7, the valve 8, and the throttle 9, returns to the secondary side of the heat exchanger 7, and then enters the gas-liquid separator 101. .

ここで分離された液冷媒は絞り102を経てエバポレー
タ4へ流れ、ガス冷媒は絞り103を経て流点10でエ
バポレータ4を流過した冷媒と混合して圧縮機1に吸込
まれる。容量制御をしないときは、圧縮機1の吐出ガス
は、コンデンサ2、膨張弁3を通りエバポレータ4から
圧縮機1に戻る。
The liquid refrigerant separated here flows to the evaporator 4 through the throttle 102, and the gas refrigerant passes through the throttle 103 and mixes with the refrigerant that has flowed through the evaporator 4 at a flow point 10, and is sucked into the compressor 1. When the capacity is not controlled, the gas discharged from the compressor 1 passes through the condenser 2 and the expansion valve 3 and returns to the compressor 1 from the evaporator 4.

室内の温度が低くなり、冷房能力を下げたいとき即ち容
量制御するときは、弁8を開き、コンデンサ2の中間ボ
ート6より気液混合状態の冷媒を熱交換器7の1次側に
導く。この冷媒は弁8を通り絞り9を通つて熱交換器7
の2次側へと再び導びかれる。このとき絞り9により圧
力が絞られるため冷媒の温度は低下する。この低い温度
の2次側の冷媒により1次側の冷媒が冷やされるため1
次側の温度が低くなる。熱交換器7の2次側より出た気
液混合状態の冷媒は気液分離器101により気液離され
る。気液分離された冷媒のうち液冷媒は絞り102を通
つてエバポレータ4へ導かれる。一方コンデンサ2内の
冷媒の残部は膨張弁3を通つてエバポレータ4。へ導か
れる。従つてエバポレータ4を流れる冷媒量は気液分離
器101、絞り102を通る冷媒と22膨張弁3を通る
冷媒の和となるが、気液分離器101て分離されたガス
冷媒分だけ容量制御しない場合に比べ少なくなり、室内
の冷房能力が小さくなる。一方コンデンサ中間ボート6
より後のコンデンサ2の流量は少なくなるので、コンデ
ンサ2の冷却効果が良くなり全体的にコンデンサ2の冷
媒温度が低くなると同時に、熱交換器7を流過した冷媒
の温度も低くなり、圧縮機1の吐出圧力は冷媒凝縮温度
に対応した圧力になるので圧縮機1の吐出圧力が低くな
る。
When the indoor temperature becomes low and it is desired to lower the cooling capacity, that is, to control the capacity, the valve 8 is opened and the refrigerant in a gas-liquid mixed state is guided from the intermediate boat 6 of the condenser 2 to the primary side of the heat exchanger 7. This refrigerant passes through a valve 8 and a restrictor 9 into a heat exchanger 7.
is again guided to the secondary side of At this time, since the pressure is throttled by the throttle 9, the temperature of the refrigerant decreases. Because the primary side refrigerant is cooled by this low temperature secondary side refrigerant, 1
The temperature on the next side becomes lower. The refrigerant in a gas-liquid mixed state discharged from the secondary side of the heat exchanger 7 is separated into gas-liquid by a gas-liquid separator 101. Of the refrigerant separated into gas and liquid, the liquid refrigerant is guided to the evaporator 4 through the throttle 102 . On the other hand, the remainder of the refrigerant in the condenser 2 passes through an expansion valve 3 to an evaporator 4. be led to. Therefore, the amount of refrigerant flowing through the evaporator 4 is the sum of the refrigerant passing through the gas-liquid separator 101, the throttle 102, and the refrigerant passing through the expansion valve 22, but the capacity is not controlled by the amount of gas refrigerant separated by the gas-liquid separator 101. This will reduce the indoor cooling capacity. On the other hand, the capacitor intermediate boat 6
Since the flow rate of the later condenser 2 is smaller, the cooling effect of the condenser 2 is improved and the refrigerant temperature of the condenser 2 is lowered overall.At the same time, the temperature of the refrigerant that has passed through the heat exchanger 7 is also lowered, and the Since the discharge pressure of compressor 1 corresponds to the refrigerant condensation temperature, the discharge pressure of compressor 1 becomes low.

なおこのときの圧縮機1の吸込み圧力は、大きく変化し
ないため、圧縮機1の・圧縮比は小さくなり、圧縮機1
を駆動する原動機5の動力も小さくなる。かくして室内
の冷房負荷の低下に応じて圧縮機1の動力も小さくなる
。なお、以上の説明ては絞り102は固定絞りであつた
が、これを可変絞りとし、室温を検知してこの信号によ
り絞り102の絞り度合を制御しエバポレータ4へ流す
冷媒量を調整することにより、室温の制御を滑らかに行
なうことができる。圧縮機1を0N−OFF制御して室
内の温度を調節すると、室内の温度変化が大きくなるが
、本発明のようにエバポレータ4への冷媒流量を変える
ことにより冷房能力を制御すると、室内の温度を精度よ
く一定にすることができる。なお、このとき圧縮機1の
動力も小さくなりその成績係数も大きく低下することが
なく、気液分離器101の作用により圧縮機1の液圧縮
を防止することができ、圧縮機の液圧縮による損傷を防
止することができる。
Note that the suction pressure of the compressor 1 at this time does not change significantly, so the compression ratio of the compressor 1 becomes small, and the compressor 1
The power of the prime mover 5 that drives the motor 5 also becomes smaller. Thus, as the indoor cooling load decreases, the power of the compressor 1 also decreases. In the above explanation, the diaphragm 102 was a fixed diaphragm, but by making it a variable diaphragm, detecting the room temperature and controlling the degree of diaphragm 102 based on this signal, the amount of refrigerant flowing to the evaporator 4 can be adjusted. , room temperature can be controlled smoothly. If the indoor temperature is adjusted by controlling the compressor 1 to 0N-OFF, the indoor temperature will change greatly, but if the cooling capacity is controlled by changing the refrigerant flow rate to the evaporator 4 as in the present invention, the indoor temperature will change. can be kept constant with high precision. At this time, the power of the compressor 1 also decreases, and its coefficient of performance does not decrease significantly, and the action of the gas-liquid separator 101 prevents the compressor 1 from compressing the liquid. Damage can be prevented.

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

第1図は従来の空気調和機の冷媒系統図、第2図は本発
明の1実施例を示す冷媒系統図である。
FIG. 1 is a refrigerant system diagram of a conventional air conditioner, and FIG. 2 is a refrigerant system diagram showing one embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1 コンデンサの中間ポートから抽出した冷媒を熱交換
器の1次側、コントロール弁、絞りを通つて再び上記熱
交換器の2次側、そして圧縮機に戻すバイパス系統を具
えた冷凍サイクルにおいて、上記バイパス系統の熱交換
器下流側に気液分離器を設け、ここで分離した冷媒ガス
を圧縮機に、液冷媒をエバポレータの入口に流入させる
ようにしたことを特徴とする冷凍サイクル。
1. In a refrigeration cycle equipped with a bypass system in which the refrigerant extracted from the intermediate port of the condenser is returned through the primary side of the heat exchanger, a control valve, and a throttle, to the secondary side of the heat exchanger, and then to the compressor. A refrigeration cycle characterized in that a gas-liquid separator is provided downstream of a heat exchanger in a bypass system, and the refrigerant gas separated there flows into a compressor and the liquid refrigerant flows into an inlet of an evaporator.
JP14363779A 1979-11-06 1979-11-06 refrigeration cycle Expired JPS6056980B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14363779A JPS6056980B2 (en) 1979-11-06 1979-11-06 refrigeration cycle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14363779A JPS6056980B2 (en) 1979-11-06 1979-11-06 refrigeration cycle

Publications (2)

Publication Number Publication Date
JPS5668754A JPS5668754A (en) 1981-06-09
JPS6056980B2 true JPS6056980B2 (en) 1985-12-12

Family

ID=15343390

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14363779A Expired JPS6056980B2 (en) 1979-11-06 1979-11-06 refrigeration cycle

Country Status (1)

Country Link
JP (1) JPS6056980B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2501811B2 (en) * 1987-01-27 1996-05-29 富士電機株式会社 Refrigeration equipment
JP4631426B2 (en) * 2004-12-21 2011-02-16 株式会社デンソー Vapor compression refrigerator

Also Published As

Publication number Publication date
JPS5668754A (en) 1981-06-09

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