JPS62245058A - Flow diverter - Google Patents
Flow diverterInfo
- Publication number
- JPS62245058A JPS62245058A JP61088548A JP8854886A JPS62245058A JP S62245058 A JPS62245058 A JP S62245058A JP 61088548 A JP61088548 A JP 61088548A JP 8854886 A JP8854886 A JP 8854886A JP S62245058 A JPS62245058 A JP S62245058A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- evaporator
- container
- liquid
- flow rate
- 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.)
- Granted
Links
- 239000007788 liquid Substances 0.000 claims description 10
- 239000003507 refrigerant Substances 0.000 description 30
- 230000004907 flux Effects 0.000 description 8
- 238000005057 refrigeration Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Landscapes
- Glass Compositions (AREA)
- Valve Device For Special Equipments (AREA)
- Valve-Gear Or Valve Arrangements (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (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
本発明は冷蔵庫、空調機等に用いられる冷凍サイクルの
分流器に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a flow divider for a refrigeration cycle used in refrigerators, air conditioners, etc.
従来の技術
従来、この種の冷凍サイクルは第2図に示すように、圧
縮機1.凝縮器2.受液器3.同一抵抗の絞り4.蒸発
器6を配管で環状に連結して構成されている。そして、
蒸発器6の冷媒側圧力損失をできる限り小さくする為に
冷媒回路数を複数にし、したがって同一抵抗の絞り4も
冷媒回路数に合わせて複数個設けている。このような構
成において、蒸発器6には矢印6方向に空気が流動し冷
媒と熱交換を行う。BACKGROUND OF THE INVENTION Conventionally, this type of refrigeration cycle has a compressor 1, as shown in FIG. Condenser 2. Receiver 3. Aperture with the same resistance 4. It is constructed by connecting evaporators 6 in an annular manner through piping. and,
In order to reduce the pressure loss on the refrigerant side of the evaporator 6 as much as possible, a plurality of refrigerant circuits are provided, and accordingly, a plurality of throttles 4 having the same resistance are provided in accordance with the number of refrigerant circuits. In such a configuration, air flows in the evaporator 6 in the direction of the arrow 6 and exchanges heat with the refrigerant.
発明が解決しようとする問題点
しかし、このような構成のものでは、絞り4の抵抗をか
えても通常の冷凍サイクルでは臨界流になっており流量
はかえられない。また蒸発器5において熱交換されない
新鮮な空気が入る部分すなわち風上側の伝熱管にも、熱
交換された空気が入る部分すなわち風下側の伝熱管にも
同一抵抗の絞り4によって等流量の冷媒が流入する。し
たがって、熱流束の大きい風上側では冷媒は蒸発しやす
ぐガス域が長くなり伝熱性能が低下するという問題があ
った。Problems to be Solved by the Invention However, with such a configuration, even if the resistance of the throttle 4 is changed, in a normal refrigeration cycle, the flow becomes a critical flow and the flow rate cannot be changed. Furthermore, in the evaporator 5, an equal flow rate of refrigerant is applied to the part of the evaporator 5 where fresh air that is not subjected to heat exchange enters, that is, the windward side heat transfer tube, and the part where heat exchanged air enters, that is, the leeward side heat transfer tube, by the aperture 4 having the same resistance. Inflow. Therefore, on the windward side where the heat flux is large, the refrigerant evaporates quickly and the gas region becomes long, resulting in a problem that heat transfer performance deteriorates.
問題点を解決する為の手段
本発明は上記のような問題点を解決する。すなわち蒸発
器の複数の冷媒回路にそれぞれの熱流束に応じて冷媒流
量を流す為に、気体と液体を分離する容器に、一端が気
体側に開放され他端が蒸発器に連結される複数の管を設
け、この複数の管の液体側の管壁に設けた孔を前記容器
底からの高さが異なるように配設した分流器を冷凍サイ
クルにとりつけるものである。Means for Solving the Problems The present invention solves the problems as described above. In other words, in order to flow a refrigerant flow rate in accordance with the heat flux of each refrigerant circuit to the multiple refrigerant circuits of the evaporator, a plurality of refrigerant circuits, one end of which is open to the gas side and the other end of which is connected to the evaporator, are installed in a container that separates gas and liquid. A flow divider is attached to a refrigeration cycle, in which a plurality of tubes are provided, and holes formed in the tube wall on the liquid side of the plurality of tubes are arranged at different heights from the bottom of the container.
作用
このような技術的手段により、容器内の液面と孔のヘッ
ド差に応じて蒸発器への冷媒流量を制御することができ
るので、蒸発器の各冷媒回路で効率良く冷媒を蒸発させ
ることができるので熱交換性能金著しく向上させること
ができる。Effect: With such technical means, the flow rate of refrigerant to the evaporator can be controlled according to the head difference between the liquid level in the container and the hole, so that the refrigerant can be efficiently evaporated in each refrigerant circuit of the evaporator. As a result, heat exchange performance can be significantly improved.
実施例 以下1本発明の一実施例を第1図に基づいて説明する。Example An embodiment of the present invention will be described below with reference to FIG.
圧縮機7.凝縮器8.絞り91分流器10゜蒸発器11
を冷媒配管12で環状に連結して冷凍サイクルを構成し
ている。蒸発器11は冷媒の圧力損失をできる限り小さ
くする為に本実施例では冷媒回路を3回路13,14.
15にしている。Compressor7. Condenser8. Throttle 91 Divider 10° Evaporator 11
are connected in an annular manner by a refrigerant pipe 12 to form a refrigeration cycle. In order to minimize the pressure loss of the refrigerant, the evaporator 11 has three refrigerant circuits 13, 14 .
I set it to 15.
また1分流器1oは気体16と液体17を分離する容器
になっており、この容器内には蒸発器11の冷媒回路数
に応じて3本の管18,19.20を一端が気体16側
に開放され他端が蒸発器11の各冷媒回路13,14.
15に連結するように設置しており、この各管18 、
19 、20の液体17側の管壁には各々同径の孔21
,22.23を設け、しかも容器1o底からの高さ全2
1.22゜23の順に高くしである。なお、24は管1
8゜19 、20の気体側開放端に絞り9を通過してき
た冷媒液が流入しないように設けたバッフル板である。In addition, the flow divider 1o is a container that separates the gas 16 and the liquid 17, and in this container there are three pipes 18, 19, 20, one end of which is on the gas 16 side, depending on the number of refrigerant circuits of the evaporator 11. The other end is open to each refrigerant circuit 13, 14 .
15, and each of these pipes 18,
19 and 20 have holes 21 of the same diameter in the tube walls on the liquid 17 side.
, 22.23, and the total height from the bottom of container 1o is 2.
The height increases in the order of 1.22°23. In addition, 24 is tube 1
This is a baffle plate provided at the gas side open ends of 8°19 and 20 to prevent the refrigerant liquid that has passed through the throttle 9 from flowing into the gas side open ends.
また、蒸発器11には送風機(図示せず)により矢印2
5方向に空気流が流動する。Further, the evaporator 11 is provided with an arrow 2 by a blower (not shown).
Air flows in five directions.
次に、この一実施例の構成における作用を説明する。蒸
発器11の冷媒回路においては風上側から順番に、すな
わち13,14.15の順番に熱流束が小さくなる。Next, the operation of the configuration of this embodiment will be explained. In the refrigerant circuit of the evaporator 11, the heat flux decreases in order from the windward side, that is, in the order of 13, 14, and 15.
一方、分流器10においては、管20,19゜18の順
番にヘッド差が大きいので冷媒流量も管20.19.1
8の順番に多くなる。On the other hand, in the flow divider 10, since the head difference is larger in the order of pipes 20, 19, 18, the refrigerant flow rate is also larger in the order of pipes 20, 19, 18.
The number increases in the order of 8.
したがって、熱流束の大きい冷媒回路13には冷媒流量
が多く、熱流束の小さい冷媒回路16には冷媒流量が少
なく流れる、すなわち熱流束に応じて冷媒流量を最適に
調整することができる為。Therefore, the refrigerant flow rate is large in the refrigerant circuit 13 with a large heat flux, and the refrigerant flow rate is low in the refrigerant circuit 16 with a small heat flux, that is, the refrigerant flow rate can be optimally adjusted according to the heat flux.
各冷媒回路13,14.15毎に蒸発潜熱を有効に吸収
することができ蒸発器11の伝熱性能が著しく向上する
。The latent heat of vaporization can be effectively absorbed in each refrigerant circuit 13, 14, 15, and the heat transfer performance of the evaporator 11 is significantly improved.
なお、このように熱流束に応じて冷媒流量を変える手段
は管IEl、19.20に設けた孔21゜22.23の
容器底からの高さを同一にして、孔径を異ならせるある
いは同一孔径で孔数を異ならせても良いことは当該技術
者であれば容易に考えられる。In addition, the means to change the refrigerant flow rate according to the heat flux in this way is to make the heights of the holes 21° and 22.23 provided in the pipe IEl, 19.20 the same from the bottom of the container and have different hole diameters, or to make the holes with the same hole diameter. A person skilled in the art can easily think that the number of holes may be made different.
発明の効果
以上のように本発明の分流器は、気体と液体を分離する
容器に、一端が気体側に開放され他端が蒸発器に連結さ
れる複数の管を設け、この複数の管の液体側の管壁に設
けた孔を前記容器底からの高さが異なるように配設した
ものであるから、蒸発器各冷媒回路の熱流束に応じて冷
媒流量を制御できるので蒸発器の伝熱性能が著しぐ向上
する。Effects of the Invention As described above, in the flow divider of the present invention, a container for separating gas and liquid is provided with a plurality of tubes, one end of which is open to the gas side and the other end of which is connected to an evaporator. Since the holes in the pipe wall on the liquid side are arranged at different heights from the bottom of the container, the refrigerant flow rate can be controlled according to the heat flux of each refrigerant circuit in the evaporator, which improves the transmission of the evaporator. Thermal performance is significantly improved.
第1図は本発明の一実施例の分流器を用いた熱ポンプ装
置の構成図、第2図は従来例の分流器を用いた熱ポンプ
装置の構成図である。
10・・・・・・分流器、18〜20・・・・・・管、
21〜23・・・・・・孔。FIG. 1 is a configuration diagram of a heat pump device using a flow divider according to an embodiment of the present invention, and FIG. 2 is a configuration diagram of a heat pump device using a conventional flow divider. 10... Flow divider, 18-20... Tube,
21-23... Holes.
Claims (1)
他端が蒸発器に連結される複数の管を設け、この複数の
管の液体側の管壁に設けた孔を前記容器底からの高さが
異なるように配設した分流器。A container for separating gas and liquid is provided with a plurality of tubes with one end open to the gas side and the other end connected to an evaporator, and holes provided in the tube wall on the liquid side of the plurality of tubes are inserted from the bottom of the container. Flow dividers arranged at different heights.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61088548A JPS62245058A (en) | 1986-04-17 | 1986-04-17 | Flow diverter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61088548A JPS62245058A (en) | 1986-04-17 | 1986-04-17 | Flow diverter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62245058A true JPS62245058A (en) | 1987-10-26 |
JPH0411781B2 JPH0411781B2 (en) | 1992-03-02 |
Family
ID=13945908
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61088548A Granted JPS62245058A (en) | 1986-04-17 | 1986-04-17 | Flow diverter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62245058A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0423969U (en) * | 1990-04-02 | 1992-02-26 | ||
JPH05264115A (en) * | 1992-03-16 | 1993-10-12 | Matsushita Electric Ind Co Ltd | Absorption heat pump device |
JP2008057941A (en) * | 2006-09-04 | 2008-03-13 | Fuji Electric Retail Systems Co Ltd | Refrigerant cycle device |
WO2016121123A1 (en) * | 2015-01-30 | 2016-08-04 | 三菱電機株式会社 | Refrigeration cycle device |
-
1986
- 1986-04-17 JP JP61088548A patent/JPS62245058A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0423969U (en) * | 1990-04-02 | 1992-02-26 | ||
JPH05264115A (en) * | 1992-03-16 | 1993-10-12 | Matsushita Electric Ind Co Ltd | Absorption heat pump device |
JP2008057941A (en) * | 2006-09-04 | 2008-03-13 | Fuji Electric Retail Systems Co Ltd | Refrigerant cycle device |
WO2016121123A1 (en) * | 2015-01-30 | 2016-08-04 | 三菱電機株式会社 | Refrigeration cycle device |
Also Published As
Publication number | Publication date |
---|---|
JPH0411781B2 (en) | 1992-03-02 |
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