JPS61101776A - Refrigerant flow branching device for heat exchanger - Google Patents

Refrigerant flow branching device for heat exchanger

Info

Publication number
JPS61101776A
JPS61101776A JP59223439A JP22343984A JPS61101776A JP S61101776 A JPS61101776 A JP S61101776A JP 59223439 A JP59223439 A JP 59223439A JP 22343984 A JP22343984 A JP 22343984A JP S61101776 A JPS61101776 A JP S61101776A
Authority
JP
Japan
Prior art keywords
heat exchanger
evaporator
refrigerant
refrigerant flow
branching device
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
JP59223439A
Other languages
Japanese (ja)
Inventor
慶吾 浅山
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 Ecology Systems Co Ltd
Original Assignee
Matsushita Seiko Co 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 Matsushita Seiko Co Ltd filed Critical Matsushita Seiko Co Ltd
Priority to JP59223439A priority Critical patent/JPS61101776A/en
Publication of JPS61101776A publication Critical patent/JPS61101776A/en
Pending legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (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、冷凍サイクルを有する空気調和機の複数の熱
交換器への冷媒分流装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a refrigerant distribution device for a plurality of heat exchangers of an air conditioner having a refrigeration cycle.

従来例の構成とその問題点 一般に空気調和機の冷凍サイクルは第2図および第3図
に示すようにコンプレッサー1、室内熱交換器2、減圧
器3、液タンク4、室外熱交換器(蒸発器)5より構成
され、また、蒸発能力を大きくするために、室外側熱交
換器、すなわち蒸発器5を複数個の蒸発器6a 、sb
をもって構成し、高圧液冷媒を分流器6によって分流す
るようにしている。ところが、分流6の各蒸発器6a 
、 sbへの接続部ea、ebの間には高低差が存在す
ることから、冷媒の上下偏流による圧力差、分流状態の
悪化を招きまだ、上下蒸発器間のファンによる受風面積
の違いから生ずる蒸発器効率の偏差が存在することより
比体積の大きなガス冷媒の割合の高い蒸発器の方が、圧
力損失が大きくなり、その結果、さらに分流が悪化し、
蒸発器に冷媒を均等に分流できないという問題点を有し
ていた。また蒸発器が2台独立して構成される冷媒サイ
クルにおいて、2台の蒸発器の内蒸発器6aを強風。
Conventional structure and its problems In general, the refrigeration cycle of an air conditioner consists of a compressor 1, an indoor heat exchanger 2, a pressure reducer 3, a liquid tank 4, an outdoor heat exchanger (evaporation In addition, in order to increase the evaporation capacity, the outdoor heat exchanger, that is, the evaporator 5, is constructed of a plurality of evaporators 6a, sb.
The high-pressure liquid refrigerant is divided by a flow divider 6. However, each evaporator 6a of the branch 6
, Since there is a height difference between the connection parts ea and eb to sb, this causes a pressure difference due to the vertical drift of the refrigerant and worsens the divided flow condition. Due to the deviation in evaporator efficiency that occurs, an evaporator with a high proportion of gas refrigerant with a large specific volume will have a larger pressure loss, which will further worsen the shunt flow.
There was a problem in that the refrigerant could not be distributed evenly to the evaporator. In addition, in a refrigerant cycle configured with two independent evaporators, strong wind blows through the evaporator 6a of the two evaporators.

蒸発器6bを微風で動作させると、蒸発器6aの方が蒸
発能力が大きなため、蒸発器5b内では、比体積の大き
な気体冷媒となる。ところが、分流器6と合流器7にお
ける圧力P6. P7ば、能力の差異ばかかわらず共通
であるから、蒸発器5aと蒸発器5bは、圧力損失ΔP
5a+Δ”sbが相互に等しくなるように分流するため
、蒸発器5aの分流冷媒は、蒸発器5bと比較すると重
−i、を流量では少なくなり1分流状態の悪化を招くと
いう問題点を有していた。また分流器6はその設置方法
の差異による分流偏差が大きいという事例も報告されて
いる。
When the evaporator 6b is operated with a light breeze, the evaporator 6a has a larger evaporation capacity, so the refrigerant becomes a gaseous refrigerant with a large specific volume in the evaporator 5b. However, the pressure P6. Since P7 is common regardless of the difference in capacity, the pressure loss ΔP of the evaporators 5a and 5b is
Since the flow is divided so that 5a+Δ"sb is mutually equal, the divided refrigerant in the evaporator 5a has a problem that the flow rate of the refrigerant is lower than that in the evaporator 5b, causing deterioration of the divided flow condition. It has also been reported that the shunt 6 has a large deviation in shunt flow due to differences in its installation method.

発明の目的 本発明は上記問題点を解決するために、本発明は圧力損
失偏差が少なく、良好な分流状態であり、しかも低価格
である熱交換器の冷媒分流装置を提供するものである。
OBJECTS OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a refrigerant distribution device for a heat exchanger that has a small pressure loss deviation, has a good distribution condition, and is inexpensive.

発明の構成 この目的を達成するため本発明は、空気調和機の複数の
熱交換器の入口を冷媒分流管にて相互に配管接続し、熱
交換器内の圧力損失偏差を抑えている。
Structure of the Invention To achieve this object, the present invention connects the inlets of a plurality of heat exchangers of an air conditioner to each other via refrigerant distribution pipes, thereby suppressing pressure loss deviation within the heat exchangers.

実施例の説明 以下、第1図に基づいて本発明の一実施例について説明
する。以下、従来例と構成が同じものには同一符号を付
与して説明は省略する。
DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. Hereinafter, components having the same configuration as the conventional example will be given the same reference numerals and the description will be omitted.

暖房時、減圧器3を通った高圧液冷媒は、液タンク4を
介して蒸発器5a 、sb入口の分流器6に送られる。
During heating, the high-pressure liquid refrigerant that has passed through the pressure reducer 3 is sent via the liquid tank 4 to the evaporator 5a and the flow divider 6 at the sb inlet.

分流された冷媒は、各蒸発器の入口sa、、ebに送ら
れる。ここで蒸発器5a 、 sbの間に圧力差が存在
し、蒸発器内の圧力損失ΔP5a+ΔP5bが異なった
としても蒸発器人口6a、6b、 を冷媒分流管10に
て配管接続している事により、圧力の高い方から低い方
への流れが生じ、圧力量を緩和し、圧力損失を等しくす
る。
The divided refrigerant is sent to the inlets sa, eb of each evaporator. Here, even if there is a pressure difference between the evaporators 5a and sb and the pressure loss ΔP5a+ΔP5b within the evaporators is different, by connecting the evaporators 6a, 6b with the refrigerant distribution pipe 10, Flow occurs from the higher pressure side to the lower pressure side, relieving the amount of pressure and equalizing the pressure loss.

この方法を多室対応型空気調和機の室外熱交換器に使用
すれば、従来の配管と比べ蒸発器人口6a。
If this method is used for the outdoor heat exchanger of a multi-room air conditioner, the evaporator population will be 6a compared to conventional piping.

6bでの温度偏差は20〜30%減少し、圧力偏差では
、約半分に減少し、蒸発器出口における過熱度偏差は約
30係減少する。なお冷媒分流管10は、毛細管でも良
く、要は熱交換器入口相互間を連通したものであれば良
い。
The temperature deviation at 6b is reduced by 20-30%, the pressure deviation is reduced by about half, and the superheat deviation at the evaporator outlet is reduced by about a factor of 30. Note that the refrigerant distribution tube 10 may be a capillary tube, as long as it communicates between the inlets of the heat exchanger.

発明の効果 このように本発明の熱交換器の冷媒分流装置は、熱交換
の圧力損失偏差を冷媒分流管を設けることによって少な
くし、良好な冷媒分流を安価に提供できるものとしてい
る。
Effects of the Invention As described above, the refrigerant distribution device for a heat exchanger of the present invention reduces the pressure loss deviation during heat exchange by providing a refrigerant distribution pipe, and can provide good refrigerant distribution at a low cost.

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

第1図は本発明一実施例の蒸発器の要部斜視図、第2図
は、空気調和機の冷凍サイクル図、第3図は、従来の空
気調和機に用いられている蒸発器の要部斜視図である。 sa、5b・・・・・・蒸発器、6a、eb・・・・・
・蒸発器入口、10−・・・・冷媒分流管。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
Fig. 1 is a perspective view of essential parts of an evaporator according to an embodiment of the present invention, Fig. 2 is a refrigeration cycle diagram of an air conditioner, and Fig. 3 is a main part of an evaporator used in a conventional air conditioner. FIG. sa, 5b...evaporator, 6a, eb...
- Evaporator inlet, 10-... Refrigerant distribution pipe. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
figure

Claims (1)

【特許請求の範囲】[Claims]  冷凍サイクルを有する空気調和機の複数熱交換器入口
間を冷媒分流管にて相互に配管接続した熱交換器の冷媒
分流装置。
A refrigerant distribution device for a heat exchanger in which multiple heat exchanger inlets of an air conditioner having a refrigeration cycle are interconnected by refrigerant distribution tubes.
JP59223439A 1984-10-23 1984-10-23 Refrigerant flow branching device for heat exchanger Pending JPS61101776A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59223439A JPS61101776A (en) 1984-10-23 1984-10-23 Refrigerant flow branching device for heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59223439A JPS61101776A (en) 1984-10-23 1984-10-23 Refrigerant flow branching device for heat exchanger

Publications (1)

Publication Number Publication Date
JPS61101776A true JPS61101776A (en) 1986-05-20

Family

ID=16798159

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59223439A Pending JPS61101776A (en) 1984-10-23 1984-10-23 Refrigerant flow branching device for heat exchanger

Country Status (1)

Country Link
JP (1) JPS61101776A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09101746A (en) * 1995-10-05 1997-04-15 Toppan Printing Co Ltd Map or map collection
JP2009153750A (en) * 2007-12-27 2009-07-16 Techmatrix Corp Medical image display apparatus and medical image display method
JP2015055406A (en) * 2013-09-11 2015-03-23 ダイキン工業株式会社 Heat exchanger
WO2019058540A1 (en) * 2017-09-25 2019-03-28 三菱電機株式会社 Refrigerant distributor and air-conditioning device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57137974U (en) * 1981-02-19 1982-08-28
JPS5853359A (en) * 1981-09-25 1983-03-29 Kawasaki Steel Corp Sequential continuous casting method for dissimilar kinds of steel

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57137974U (en) * 1981-02-19 1982-08-28
JPS5853359A (en) * 1981-09-25 1983-03-29 Kawasaki Steel Corp Sequential continuous casting method for dissimilar kinds of steel

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09101746A (en) * 1995-10-05 1997-04-15 Toppan Printing Co Ltd Map or map collection
JP2009153750A (en) * 2007-12-27 2009-07-16 Techmatrix Corp Medical image display apparatus and medical image display method
JP2015055406A (en) * 2013-09-11 2015-03-23 ダイキン工業株式会社 Heat exchanger
WO2019058540A1 (en) * 2017-09-25 2019-03-28 三菱電機株式会社 Refrigerant distributor and air-conditioning device
JPWO2019058540A1 (en) * 2017-09-25 2020-01-23 三菱電機株式会社 Refrigerant distributor and air conditioner

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