JPH0814443B2 - Gas-liquid two-phase fluid distributor - Google Patents
Gas-liquid two-phase fluid distributorInfo
- Publication number
- JPH0814443B2 JPH0814443B2 JP1252630A JP25263089A JPH0814443B2 JP H0814443 B2 JPH0814443 B2 JP H0814443B2 JP 1252630 A JP1252630 A JP 1252630A JP 25263089 A JP25263089 A JP 25263089A JP H0814443 B2 JPH0814443 B2 JP H0814443B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- outflow
- gas
- phase fluid
- phase
- 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 - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
- F25B41/42—Arrangements for diverging or converging flows, e.g. branch lines or junctions
- F25B41/45—Arrangements for diverging or converging flows, e.g. branch lines or junctions for flow control on the upstream side of the diverging point, e.g. with spiral structure for generating turbulence
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
- F25B39/028—Evaporators having distributing means
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は,空調機,冷蔵庫等に用いられる冷凍サイ
クルにおける冷媒の気相/液相二相流体の分配器に関
し,特に液相の分配比率を任意に設定できる気液二相流
体分配器に関するものである。Description: TECHNICAL FIELD The present invention relates to a vapor / liquid two-phase fluid distributor of a refrigerant in a refrigerating cycle used for an air conditioner, a refrigerator, etc., and particularly to a liquid phase distribution ratio. The present invention relates to a gas-liquid two-phase fluid distributor that can be set arbitrarily.
第8図は例えば特開昭64−58998号公報に示された従
来の気液二相流体分配器の断面と気液二相流体の流れを
示す断面図であり,図において,(11)は2方向に分流
するためのUバンド形状の管であり,その曲部中央で流
入管(2)と接続されている。そして流入管(2)の片
方の先端は,管(11)に挿入され,2方向流へ連通するよ
うに直径方向に対となる小孔(15a),(15b)が設けら
れている。FIG. 8 is a cross-sectional view of a conventional gas-liquid two-phase fluid distributor and a flow of gas-liquid two-phase fluid disclosed in, for example, Japanese Patent Laid-Open No. 64-58998, in which (11) indicates It is a U-band shaped pipe for diversion in two directions, and is connected to the inflow pipe (2) at the center of the curved portion. One end of the inflow pipe (2) is inserted into the pipe (11) and is provided with small holes (15a) and (15b) which are paired in the diameter direction so as to communicate with the bidirectional flow.
気液二相流体(10)は気相部(10a)と液相部(10b)
に分離しながら流入管に入り,矢印(14a),(14b)に
分流される。Gas-liquid two-phase fluid (10) consists of gas phase (10a) and liquid phase (10b)
While entering the inflow pipe while being separated, the flow is divided into arrows (14a) and (14b).
次に動作について説明する。 Next, the operation will be described.
気液二相流体(10)は気相部(10a)と液相部(10b)
に分離して流入管(2)に入つていき,管(11)によつ
て分流される。このとき,流入管(2)に設けられた管
(11)の曲げ方向と同じ直径方向に対となる小孔(15
a),(15b)により,気液二相流体は急激な圧力損失の
ため一部の液相の蒸発を伴いながら再混合され,小孔
(15a),(15b)から噴霧状となり噴出される。Gas-liquid two-phase fluid (10) consists of gas phase (10a) and liquid phase (10b)
It separates into the inflow pipe (2) and is divided by the pipe (11). At this time, the small holes (15) forming a pair in the same diameter direction as the bending direction of the pipe (11) provided in the inflow pipe (2).
Due to a) and (15b), the gas-liquid two-phase fluid is remixed due to the sudden pressure loss, accompanied by evaporation of a part of the liquid phase, and is ejected in the form of a spray from the small holes (15a) and (15b). .
上記のような構成の従来の気液二相流体分配器にあつ
ては,気相と液相を均一にして分配できるが,液相の分
配比率を任意に設定することが困難であるという問題点
があつた。In the conventional gas-liquid two-phase fluid distributor configured as described above, the gas phase and the liquid phase can be uniformly distributed, but it is difficult to set the distribution ratio of the liquid phase to any desired value. There was a point.
この発明は上記のような問題点を解消するためになさ
れたもので,気液二相流体分配時の液相の分配比率を任
意に設定できる気液二相流体分配器を得ることを目的と
する。The present invention has been made to solve the above problems, and an object of the present invention is to obtain a gas-liquid two-phase fluid distributor capable of arbitrarily setting the distribution ratio of the liquid phase during gas-liquid two-phase fluid distribution. To do.
この発明の気液二相流体分配器は,上部に流入管,下
部に複数の流出管を設けた分配器本体,この分配器本体
内部に上下両端部を開放して配設され,内部に上記流入
管より流入した気液二相流体の気相流体が流通する気相
流路を形成する筒状体,上記分配器本体内周壁と上記筒
状体下端部に当接して上記分配器本体を仕切り,複数の
液流出孔を有する仕切板,及びこの仕切板より下方の分
配器本体内空間を分割する分割板を備え,上記各流出管
に連通する上記液流出孔の面積を変えることにより上記
各流出管から流出する液相流体の流量を制御するように
したものである。A gas-liquid two-phase fluid distributor according to the present invention is provided with an inflow pipe in an upper portion and a plurality of outflow pipes in a lower portion, a distributor main body, and upper and lower end portions are opened inside the distributor main body. A tubular body that forms a vapor-phase flow path through which a vapor-phase fluid of a gas-liquid two-phase fluid that has flowed in from an inflow pipe is formed, and the distributor main body is brought into contact with the inner peripheral wall of the distributor main body and the lower end of the tubular body, A partition, a partition plate having a plurality of liquid outflow holes, and a partition plate that divides the space inside the distributor body below the partition plate are provided. The flow rate of the liquid phase fluid flowing out from each outflow pipe is controlled.
この発明においては,流入した気液二相流体は重力の
作用で分離され液相流体(以下,液と略記する)は分配
器本体と筒状体との間の仕切板上空間に溜まり,液流出
孔を通つて流出管に流出する。この際,例えば分割板の
形状を変えて各流出管へ連通している液流出孔の数を変
えることにより,液流出孔の総面積を変えて各流出管か
ら流出する液相流量を任意に設定することができる。In the present invention, the inflowing gas-liquid two-phase fluid is separated by the action of gravity, and the liquid-phase fluid (hereinafter abbreviated as liquid) collects in the space above the partition plate between the distributor main body and the tubular body, It flows out into the outflow pipe through the outflow hole. At this time, for example, by changing the shape of the dividing plate and changing the number of liquid outflow holes communicating with each outflow pipe, the total area of the liquid outflow holes is changed to arbitrarily change the liquid phase flow rate flowing out from each outflow pipe. Can be set.
以下,この発明の実施例を図について説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第1図はこの発明の一実施例の気液二相流体分配器の
構成を示すもので,一部切欠いて内部を示す斜視図であ
る。図において,(1)は分配器本体で,この場合は円
筒容器,(2)はこの円筒容器(1)の上部に設けられ
た流入管,(3a),(3b)は円筒容器(1)の下部,こ
の場合は底に設けられた流出管,(4)は円筒容器
(1)内に上下両端部を開放して配設された筒状体で,
この場合は円筒で気相流体が流通する気相流路(4a)を
形成している。(5)は円筒容器(1)内周壁と筒状体
(4)下端部に当接し円筒容器(1)を仕切る仕切板,
(6)は仕切板に複数穿設された液流出孔で,この場合
は12個の同一径の流出孔,(7)は仕切板(5)より下
方の円筒容器(1)内空間を分割する分割板である。FIG. 1 shows the structure of a gas-liquid two-phase fluid distributor according to one embodiment of the present invention, and is a perspective view showing the inside with a part cut away. In the figure, (1) is a distributor body, in this case, a cylindrical container, (2) is an inflow pipe provided on the upper part of this cylindrical container (1), (3a), (3b) are cylindrical containers (1) The outflow pipe provided in the lower part of the container, in this case, the bottom, and (4) is a cylindrical body arranged in the cylindrical container (1) with both upper and lower ends open,
In this case, a cylinder forms a gas-phase flow path (4a) through which the gas-phase fluid flows. (5) is a partition plate that abuts the inner peripheral wall of the cylindrical container (1) and the lower end of the tubular body (4) to partition the cylindrical container (1),
(6) is a plurality of liquid outflow holes bored in the partition plate, in this case, 12 outflow holes of the same diameter, (7) is the space inside the cylindrical container (1) below the partition plate (5) It is a dividing plate.
また,第2図はこの一実施例の縦断面図で,気液二相
流体の流れを示しており,図において,(10)は気液二
相流体,(10a)は気相,(10b)は液相を示し,二重線
矢印で気液二相流体の流れ,実線矢印で気相流体の流れ
を表わしている。第3図は同横断面図で,12個の液流出
孔(6)と分割板(7)及び流出管(3a),(3b)の位
置関係を表わしており,この実施例では,2本の流出管
(3a),(3b)には,それぞれ6個の同一径の液流出孔
(6a),(6b),…が連通している。Further, FIG. 2 is a longitudinal sectional view of this embodiment, showing the flow of a gas-liquid two-phase fluid. In the figure, (10) is a gas-liquid two-phase fluid, (10a) is a gas phase, and (10b ) Indicates the liquid phase, and the double-line arrow indicates the flow of gas-liquid two-phase fluid, and the solid line arrow indicates the flow of gas-phase fluid. FIG. 3 is a cross-sectional view showing the positional relationship between the 12 liquid outflow holes (6), the dividing plate (7), and the outflow pipes (3a) and (3b). In this embodiment, two liquid outflow holes (6) The six outflow pipes (3a) and (3b) communicate with six liquid outflow holes (6a), (6b), ...
流入管(2)から円筒容器(1)内に流入した気液二
相流体(10)(気相部(10a)+液相部(10b))は,仕
切板(5)より上部の円筒容器(1)内周壁と筒状体
(4)外壁の間の環状部空間内で重力の影響により分離
し,この環状部空間下部に溜まり液面が形成される。こ
の液は,仕切板(5)に穿設された液流出孔(6)を通
つて,流出管(3a),(3b)に流出する。このとき,各
液流出孔(6)は同一径であり,また仕切板(5)は水
平になるように配設しており,液面と各液流出孔(6)
とのヘツド差も等しいため,各液流出孔を通過する液流
量はすべて等しい。The gas-liquid two-phase fluid (10) (gas phase part (10a) + liquid phase part (10b)) flowing into the cylindrical container (1) from the inflow pipe (2) is a cylindrical container above the partition plate (5). (1) In the annular space between the inner peripheral wall and the outer wall of the tubular body (4), they are separated by the effect of gravity, and a liquid level is formed in the lower part of the annular space. This liquid flows out to the outflow pipes (3a) and (3b) through the liquid outflow hole (6) formed in the partition plate (5). At this time, each liquid outflow hole (6) has the same diameter, and the partition plate (5) is arranged horizontally so that the liquid surface and each liquid outflow hole (6)
Since the head difference is also the same, the liquid flow rate through each liquid outflow hole is the same.
したがつて,分割板(7)の形状を変えて,各流出管
(3a),(3b)と連通する液流出孔(6)の数を変える
ことによつて,液相の分配比率を設定することができ
る。Therefore, the distribution ratio of the liquid phase is set by changing the shape of the dividing plate (7) and changing the number of the liquid outflow holes (6) communicating with the outflow pipes (3a) and (3b). can do.
第3図に示したこの実施例では,各流出管(3a),
(3b)にそれぞれ6個の液流出孔(6)が連通している
ので,流出管(3a)と流出管(3b)から流出する液流量
は等しくなる。In this embodiment shown in FIG. 3, each outflow pipe (3a),
Since six liquid outflow holes (6) communicate with (3b) respectively, the liquid flow rates flowing out from the outflow pipe (3a) and the outflow pipe (3b) become equal.
一方,円筒容器(1)に流入した気相(10a)は,第
2図の矢印が示すように,気相流路(4)を通つて,各
流出管(3a),(3b)へ流出する。On the other hand, the gas phase (10a) that has flowed into the cylindrical container (1) passes through the gas phase flow path (4) and flows out to each outflow pipe (3a), (3b) as shown by the arrow in FIG. To do.
なお,上記実施例では,液を均等に2分配する気液二
相流体分配器について説明したが,第4図に示したこの
発明の他の実施例を示す横断面図では,流出管(3a)に
8個の液流出孔(6)が,流出管(3b)に4個の液流出
孔(6)が連通するように,分割板(7)を設けている
ので,流出管(3a)からの液流出量を,流出管(3b)か
らの液流出量の2倍にすることができる。In the above embodiment, the gas-liquid two-phase fluid distributor that evenly distributes the liquid is described. However, in the cross-sectional view showing another embodiment of the present invention shown in FIG. 4, the outflow pipe (3a ) Is provided with eight liquid outflow holes (6), and the outflow pipe (3b) is connected to the four liquid outflow holes (6), the dividing plate (7) is provided, so the outflow pipe (3a) The liquid outflow rate from the outflow pipe (3b) can be doubled.
また,第5図に示したこの発明のさらに他の実施例を
示す横断面図では,流出管(3a)に6個の液流出孔が,
流出管(3b)に3個の液流出孔が連通するように,仕切
板(5)に穿設した液流出孔(6a),(6b),…の間隔
を変えても,流出管(3a)からの液流出量を流出管(3
b)からの液流出量の2倍にすることができる。Further, in the transverse sectional view showing still another embodiment of the present invention shown in FIG. 5, six liquid outflow holes are formed in the outflow pipe (3a).
Even if the intervals of the liquid outflow holes (6a), (6b), ... Perforated in the partition plate (5) are changed so that the three liquid outflow holes communicate with the outflow pipe (3b), the outflow pipe (3a ) From the outflow pipe (3
It is possible to double the amount of liquid outflow from b).
また,第6図に示したこの発明のさらにまた他の実施
例を示す横断面図では,流出管(3a)に9個の液流出孔
が,流出管(3b)に3個の液流出孔が連通するように,
分割板(7)を設けているので,流出管(3a)からの液
流出量を,流出管(3b)からの液流出量の3倍にするこ
とができる。Further, in the cross-sectional view showing still another embodiment of the present invention shown in FIG. 6, nine liquid outflow holes are provided in the outflow pipe (3a) and three liquid outflow holes are provided in the outflow pipe (3b). So that they can communicate
Since the dividing plate (7) is provided, the liquid outflow amount from the outflow pipe (3a) can be made three times the liquid outflow amount from the outflow pipe (3b).
さらに,上記実施例では,気液二相流体を2分配する
分配器について示したが,第7図に示したこの発明のさ
らに他の実施例を示す断面図では,流出管を3つ設け,
流出管(3a)には4個の液流出孔が,流出管(3b)には
4個の液流出孔が,流出管(3c)には2個の液流出孔が
それぞれ連通するように,分割板(7)を設けているの
で,流出管(3a)と流出管(3b)の液流出量が,流出管
(3c)の液流出量の2倍となる3分配を行なうことがで
きる。Further, in the above embodiment, the distributor for distributing the gas-liquid two-phase fluid into two is shown, but in the sectional view showing still another embodiment of the present invention shown in FIG. 7, three outflow pipes are provided,
The outflow pipe (3a) has four liquid outflow holes, the outflow pipe (3b) has four liquid outflow holes, and the outflow pipe (3c) has two liquid outflow holes. Since the dividing plate (7) is provided, three distributions can be performed in which the liquid outflow amount of the outflow pipe (3a) and the outflow pipe (3b) is twice the liquid outflow amount of the outflow pipe (3c).
なお,上記実施例では,分割板の形状を変えて各流出
管へ連通している液流出孔の数を変えることにより,各
流出管へ連通する液流出孔の総面積を変えて各流出管か
ら流出する液流出量を制御しているが,これに限るもの
ではなく,液流出孔の孔径を異ならせてもよい。In the above-described embodiment, the total area of the liquid outflow holes communicating with each outflow pipe is changed by changing the shape of the dividing plate to change the number of liquid outflow holes communicating with each outflow pipe. Although the amount of liquid flowing out from the liquid is controlled, the present invention is not limited to this, and the diameter of the liquid outlet may be different.
また,第1図〜第3図,さらに第7図に示す実施例の
ように各流出管に均等に分配する場合,各流出管の円筒
容器(1)との連通口及び管の断面積等が等しければ,
あえて仕切板より下方の円筒容器内空間を各流出管毎に
分割板で分割する必要はない。例えば第7図に示す実施
例の場合,流出管(3c)に2個の液流出孔が連通するよ
うに分割すればよい。Further, in the case of evenly distributing to each outflow pipe as in the embodiment shown in FIGS. 1 to 3 and FIG. 7, the communication port of each outflow pipe with the cylindrical container (1) and the cross-sectional area of the pipe, etc. If they are equal,
It is not necessary to divide the inner space of the cylindrical container below the partition plate by the partition plate for each outflow pipe. For example, in the case of the embodiment shown in FIG. 7, the outflow pipe (3c) may be divided so that two liquid outflow holes communicate with each other.
さらに上記実施例では分配器本体が円筒容器の場合に
ついて示したが,四角筒等他の形状でも良い。また,筒
状体も同様である。Further, in the above embodiment, the case where the distributor main body is a cylindrical container is shown, but other shapes such as a square tube may be used. The same applies to the tubular body.
さらにまた,仕切板の液流出孔の分布(孔径,孔数)
等を変え,例えば分配器本体を形成する円筒容器を仕切
板より下で分割できる嵌め合いの上下二部材で摺動自在
に構成し,円筒容器の下方の部材を回動させることによ
り各流出管に連通する液流出孔の数等を変えて,各流出
管から流出す液流出量を自在に変えることも可能であ
る。Furthermore, distribution of liquid outflow holes on the partition plate (hole diameter, number of holes)
Etc., for example, the cylindrical container forming the distributor main body is configured to be slidable by two upper and lower members that fit together so that it can be divided below the partition plate, and each of the outflow pipes can be rotated by rotating the member below the cylindrical container. It is also possible to freely change the amount of liquid flowing out from each of the outflow pipes by changing the number of liquid outflow holes communicating with the.
以上のように,この発明によれば,上部に流入管,下
部に複数の流出管を設けた分配器本体,この分配器本体
内部に上下両端部を開放して配設され,内部に上記流入
管より流入した気液二相流体の気相流体が流通する気相
流路を形成する筒状体,上記分配器本体内周壁と上記筒
状体下端部に当接して上記分配器本体を仕切り,複数の
液流出孔を有する仕切板,及びこの仕切板より下方の分
配器本体内空間を分割する分割板を備えるものにし,上
記各流出管に連通する上記液流出孔の面積を変えること
により上記各流出管から流出する液相流体の流量を制御
するようにしたので,各流出管から流出する液相流体の
流量を任意に設定できる,すなわち分配比率を任意に設
定できる気液二相流体分配器が得られる効果がある。As described above, according to the present invention, the inflow pipe is provided in the upper part, the distributor body is provided with a plurality of outflow pipes in the lower part, and the upper and lower ends are disposed inside the distributor body, and the inflow pipe is provided inside. A tubular body that forms a gas-phase flow path through which a gas-phase fluid of a gas-liquid two-phase fluid that flows in from a pipe flows, and abuts the inner peripheral wall of the distributor body and the lower end of the tubular body to partition the distributor body. By providing a partition plate having a plurality of liquid outflow holes and a partition plate that divides the space inside the distributor body below the partition plate, by changing the area of the liquid outflow holes communicating with each of the outflow pipes. Since the flow rate of the liquid phase fluid flowing out from each of the outflow pipes is controlled, the flow rate of the liquid phase fluid flowing out of each outflow pipe can be arbitrarily set, that is, the distribution ratio can be arbitrarily set. There is an effect that a distributor can be obtained.
第1図はこの発明の一実施例の気液二相流体分配器の一
部切欠き斜視図,第2図は第1図の縦断面図,第3図は
同横断面図,第4図,第5図,第6図,第7図はこの発
明の他の実施例の気液二相流体分配器の横断面図,第8
図は従来の気液二相流体分配器を示す断面図である。 図において,(1)は分配器本体である円筒容器,
(2)は流入管,(3a),(3b),(3c)は流出管,
(4)は筒状体,(4a)は気相流路,(5)は仕切板,
(6)は液流出孔,(7)は分割板,(10)は気液二相
流体,(10a)は気相部,(10b)は液相部である。 なお,図中,同一符号は同一,又は相当部分を示す。FIG. 1 is a partially cutaway perspective view of a gas-liquid two-phase fluid distributor according to an embodiment of the present invention, FIG. 2 is a longitudinal sectional view of FIG. 1, FIG. 3 is a lateral sectional view thereof, and FIG. , FIG. 5, FIG. 6, and FIG. 7 are cross-sectional views of a gas-liquid two-phase fluid distributor according to another embodiment of the present invention, and FIG.
The figure is a cross-sectional view showing a conventional gas-liquid two-phase fluid distributor. In the figure, (1) is a cylindrical container that is the distributor body,
(2) is an inflow pipe, (3a), (3b), (3c) is an outflow pipe,
(4) is a tubular body, (4a) is a vapor phase flow path, (5) is a partition plate,
(6) is a liquid outflow hole, (7) is a dividing plate, (10) is a gas-liquid two-phase fluid, (10a) is a gas phase part, and (10b) is a liquid phase part. In the drawings, the same reference numerals indicate the same or corresponding parts.
Claims (1)
た分配器本体,この分配器本体内部に上下両端部を開放
して配設され,内部に上記流入管より流入した気液二相
流体の気相流体が流通する気相流路を形成する筒状体,
上記分配器本体内周壁と上記筒状体下端部に当接して上
記分配器本体を仕切り,複数の液流出孔を有する仕切
板,及びこの仕切板より下方の分配器本体内空間を分割
する分割板を備え,上記各流出管に連通する上記液流出
孔の面積を変えることにより上記各流出管から流出する
液相流体の流量を制御するようにした気液二相流体分配
器。1. A distributor main body having an inflow pipe in an upper part and a plurality of outflow pipes in a lower part, and a gas-liquid flowing into the inside of the distributor main body from the inflow pipe with both upper and lower ends open. A tubular body forming a gas-phase flow path through which a gas-phase fluid of two-phase fluid flows,
A partition plate that abuts the inner wall of the distributor main body and the lower end of the tubular body to partition the distributor main body and has a plurality of liquid outflow holes, and a partition that divides the space inside the distributor main body below the partition plate. A gas-liquid two-phase fluid distributor comprising a plate, wherein the flow rate of the liquid-phase fluid flowing out from each of the outflow pipes is controlled by changing the area of the liquid outflow hole communicating with each of the outflow pipes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1252630A JPH0814443B2 (en) | 1989-09-28 | 1989-09-28 | Gas-liquid two-phase fluid distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1252630A JPH0814443B2 (en) | 1989-09-28 | 1989-09-28 | Gas-liquid two-phase fluid distributor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03113251A JPH03113251A (en) | 1991-05-14 |
| JPH0814443B2 true JPH0814443B2 (en) | 1996-02-14 |
Family
ID=17240033
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1252630A Expired - Lifetime JPH0814443B2 (en) | 1989-09-28 | 1989-09-28 | Gas-liquid two-phase fluid distributor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0814443B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7261120B2 (en) | 2003-06-24 | 2007-08-28 | Morten Muller Ltd. Aps | Device for splitting a two-phase stream into two or more streams with the desired vapor/liquid ratios |
| JP5562879B2 (en) * | 2011-02-01 | 2014-07-30 | 日立アプライアンス株式会社 | Refrigerant distributor and refrigeration cycle apparatus including the same |
| JP6385871B2 (en) * | 2015-03-24 | 2018-09-05 | 日立ジョンソンコントロールズ空調株式会社 | Refrigerant distributor and refrigeration cycle apparatus equipped with the refrigerant distributor |
| WO2017221401A1 (en) * | 2016-06-24 | 2017-12-28 | 三菱電機株式会社 | Refrigerant branching distributor, heat exchanger comprising same, and refrigeration cycle device |
| JP6667070B2 (en) * | 2016-07-19 | 2020-03-18 | パナソニックIpマネジメント株式会社 | Refrigerant flow divider and refrigeration system using the same |
| KR102033350B1 (en) * | 2017-07-24 | 2019-10-17 | 엘지전자 주식회사 | Refrigerant distributor |
-
1989
- 1989-09-28 JP JP1252630A patent/JPH0814443B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03113251A (en) | 1991-05-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US7802589B2 (en) | Multirate tubing flow control valve | |
| JP3818544B2 (en) | Plate heat exchanger | |
| US5934367A (en) | Heat exchanger | |
| JPS6023210B2 (en) | flow restriction device | |
| JP2008032380A (en) | Refrigerant flow divider integrated structure expansion valve and refrigeration apparatus using the same | |
| US4775006A (en) | Heat exchanger, particularly a coolant evaporator | |
| JP2003506663A (en) | Plate heat exchanger | |
| JPH0814443B2 (en) | Gas-liquid two-phase fluid distributor | |
| JPH0737865B2 (en) | Shunt | |
| JP3390565B2 (en) | Refrigerant flow divider | |
| US5979547A (en) | Distribution device capable of uniformly distributing a medium to a plurality of tubes of a heat exchanger | |
| JPH04316785A (en) | Distributor | |
| JPH06201225A (en) | Distributor for gas-liquid two phase fluid | |
| CN212431418U (en) | Liquid separator for air conditioner and air conditioner | |
| JPH01121667A (en) | Refrigerant flow diverter | |
| JP2820428B2 (en) | Refrigerant flow divider | |
| JP2650937B2 (en) | Water cooler | |
| JPH0338598Y2 (en) | ||
| CN212431419U (en) | Liquid separator for air conditioner and air conditioner | |
| JP2516771Y2 (en) | Flow distribution adjustment tube | |
| JPH05203285A (en) | Heat exchanger | |
| JPS63221812A (en) | Shunt | |
| JPS6218795B2 (en) | ||
| JPS6259397A (en) | Vapor-liquid two-phase fluid distributor | |
| JPH05203289A (en) | Flow divider |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080214 Year of fee payment: 12 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090214 Year of fee payment: 13 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100214 Year of fee payment: 14 |
|
| EXPY | Cancellation because of completion of term | ||
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100214 Year of fee payment: 14 |