JPH03260567A - Two-phase fluid distributor for gas and liquid - Google Patents
Two-phase fluid distributor for gas and liquidInfo
- Publication number
- JPH03260567A JPH03260567A JP2055085A JP5508590A JPH03260567A JP H03260567 A JPH03260567 A JP H03260567A JP 2055085 A JP2055085 A JP 2055085A JP 5508590 A JP5508590 A JP 5508590A JP H03260567 A JPH03260567 A JP H03260567A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- gas
- distribution pipe
- phase fluid
- 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 title claims abstract description 37
- 239000012530 fluid Substances 0.000 title claims abstract description 31
- 239000012071 phase Substances 0.000 description 19
- 239000007791 liquid phase Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 230000002747 voluntary effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/0263—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by varying the geometry or cross-section of header box
-
- 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)
- Geometry (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は例えば冷凍サイクルを構成する蒸発器に、液
冷媒を均等に分配する気液二相流体の分配器に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a gas-liquid two-phase fluid distributor that evenly distributes a liquid refrigerant to an evaporator constituting a refrigeration cycle, for example.
[従来の技術]
第4図は特開昭63−220054号公報に示されたこ
の種の分配器の垂直断面図であり1図において(1)は
内部に気液二相流体を通す分配管、(2)はこの分配管
に植立させた複数の同一内径を有する分流用細管、(3
)は上記分配管(1)内の入口側に設けられ流通気液二
相流体(4)をその流れによって撹拌する回転翼である
。[Prior Art] Fig. 4 is a vertical sectional view of this type of distributor disclosed in Japanese Patent Application Laid-Open No. 63-220054. In Fig. 1, (1) is a distribution pipe through which gas-liquid two-phase fluid passes. , (2) is a plurality of diversion thin tubes with the same inner diameter planted in this distribution pipe, (3
) is a rotary blade that is installed on the inlet side of the distribution pipe (1) and stirs the flowing gas-liquid two-phase fluid (4) by its flow.
すなわち分配管(1)内に供給された気液二相流体(4
)は上記回転翼(3)により撹拌され気液混合状態とな
って、各分流用細管(2)に均等に流れるようになって
いる。In other words, the gas-liquid two-phase fluid (4) supplied into the distribution pipe (1)
) is stirred by the rotary blade (3) to form a gas-liquid mixture, which flows evenly into each of the dividing tubes (2).
[発明が解決しようとする課題]
従来の気液二相流体の分配器は以上のように構成されて
いるので、分配管内に回転翼を設ける必要があり、これ
がコスト上昇の原因となっていた。[Problem to be solved by the invention] Since the conventional gas-liquid two-phase fluid distributor is configured as described above, it is necessary to provide a rotor inside the distribution pipe, which causes an increase in cost. .
この発明は上記の問題点を解消するためになされたもの
で、上記のような回転翼を使用せずに各細管からの流出
液流量を均等にすることを目的とする。This invention was made to solve the above-mentioned problems, and its purpose is to equalize the flow rate of liquid flowing out from each capillary without using the above-mentioned rotor blades.
[課題を解決するための手段]
この発明に係る気液二相流体の分配器では、各細管の流
路抵抗は同一に設定されているが、分配管の内径を上記
流体の流れ方向に縮径させている。[Means for Solving the Problems] In the gas-liquid two-phase fluid distributor according to the present invention, the flow path resistance of each thin tube is set to be the same, but the inner diameter of the distribution tube is reduced in the flow direction of the fluid. The diameter is increased.
[作 用]
この発明における気液二相流体の分配器では、分配管の
内径がその中を通る流体の流れ方向に縮径されているの
で、液流量は均等量で各細管に分配される。[Function] In the gas-liquid two-phase fluid distributor of the present invention, the inner diameter of the distribution pipe is reduced in the direction of the flow of the fluid passing through it, so that the liquid flow rate is distributed equally to each capillary. .
[実施例]
以下この発明の一実施例について説明する。すなわち第
1図において(1)は気液二相流体が流入する分配管、
(2)はこの分配管から縦一列に分岐され同一内径を持
った複数の分流用細管、(1a)は分配管(1)の内側
室、(4)は上記分配管(1)内を通る気液二相流体、
(4a)は気相、(4b)は液相を示し。[Example] An example of the present invention will be described below. That is, in FIG. 1, (1) is a distribution pipe into which gas-liquid two-phase fluid flows;
(2) is a plurality of thin tubes for branching that are branched in a vertical line from this distribution pipe and have the same inner diameter, (1a) is the inner chamber of the distribution pipe (1), and (4) is passed through the above distribution pipe (1). gas-liquid two-phase fluid,
(4a) shows the gas phase, and (4b) shows the liquid phase.
実線矢印は気相流体の流れを表わしている。Solid arrows represent the flow of gas phase fluid.
ところで上記分配管(1)の内径は、内部を通る上記流
体の流れ方向に連続的に縮径され、下流側はど小径にな
っている点に特徴を有する。By the way, the inner diameter of the distribution pipe (1) is characterized in that it is continuously reduced in the flow direction of the fluid passing through the pipe, and has a smaller diameter on the downstream side.
また第2図は第1図の■−■拡大断面図であり、Dは分
配管(1)の内径、dは細管(2)の内径、θは分配管
(1)の中心と細管(2)の付は根の内径との威す角度
である。Fig. 2 is an enlarged sectional view taken along the line ■-■ of Fig. 1, where D is the inner diameter of the distribution tube (1), d is the inner diameter of the thin tube (2), and θ is the center of the distribution tube (1) and the thin tube (2). ) is the angle with the inner diameter of the root.
すなわち分配管(1)内に流入した気液二相流体(4)
、〔気相(4a)十液相(4b))はその内周面をほぼ
一様な液膜厚さの環状流として上昇する。このため各細
管(2)の入口を通過する液膜が、それぞれの細管(2
)へ流出することになる。そして各細管へ流出する液流
量は分配管(1)と各細管(2)の関係により次式で表
わされる。In other words, the gas-liquid two-phase fluid (4) that has flowed into the distribution pipe (1)
, [vapor phase (4a) and liquid phase (4b)] rise on the inner peripheral surface as an annular flow with a substantially uniform liquid film thickness. Therefore, the liquid film passing through the inlet of each capillary (2)
). The flow rate of liquid flowing into each capillary is expressed by the following equation based on the relationship between the distribution pipe (1) and each capillary (2).
360 DここでG
は細管からの流出液流量、Giuは流入液流量、Dは分
配管の内径、dは細管の内径、θは上記の角度である。360 D here G
is the flow rate of the outflow from the capillary, Giu is the flow rate of the inflow, D is the inner diameter of the distribution tube, d is the inner diameter of the capillary, and θ is the above angle.
したがって分配管の内径りが一様で、かつ複数の分流用
細管の内径dがすべて同じ分配器では下流側の細管はど
流入液流量が小さくなるため、流出液流量も低下するこ
とになる。Therefore, in a distributor in which the inner diameter of the distribution pipe is uniform and the inner diameter d of all the plurality of dividing thin tubes is the same, the flow rate of inflow liquid in each of the thin tubes on the downstream side will be small, and the flow rate of outflow liquid will also be reduced.
そこで第1図の実施例で示すように上記分配管(1)の
内径りを、内部を通る上記流体の流れ方向に連続的に縮
径させ、下流側はど小径にすることによって4本の細管
からの流出液流量を均等にするようにしているものであ
る。Therefore, as shown in the embodiment shown in FIG. 1, the inner diameter of the distribution pipe (1) is continuously reduced in the flow direction of the fluid passing through the interior, and the diameter on the downstream side is made smaller, so that four pipes can be connected to each other. This is intended to equalize the flow rate of liquid flowing out from the capillary.
なお上記第1図の実施例では、分配管の内径を流体の下
流側はど連続的に小さくすることによって、各細管への
流入液流量を均等にするようにした場合について説明し
たが、第3図のこの発明の他の実施例で示すように分配
管の内径を流体の下流側はど段階的に小さくしても、各
細管(2)からの流出液流量を均等にすることができる
。In the embodiment shown in FIG. 1 above, the inner diameter of the distribution pipe is continuously reduced on the downstream side of the fluid to equalize the flow rate of liquid flowing into each capillary. As shown in another embodiment of the present invention in Figure 3, even if the inner diameter of the distribution pipe is gradually reduced on the downstream side of the fluid, the flow rate of the liquid flowing out from each capillary tube (2) can be made equal. .
なお上記実施例では、気液二相流体を4分配する分配器
について説明したがこれに限るものではない、さらに上
記実施例では各細管の取付は間隔についてはふれていな
いが、この各細管の取付は間隔は細管の内径dの2倍以
上で、できるだけ大きくすればいっそう流出液流量を均
等にすることができる。Although the above embodiment describes a distributor that distributes gas-liquid two-phase fluid into four parts, the present invention is not limited to this.Furthermore, although the above embodiment does not mention the spacing between each thin tube, The mounting distance is at least twice the inner diameter d of the capillary tube, and if it is made as large as possible, the flow rate of the effluent can be made even more uniform.
[発明の効果]
この発明の気液二相流体の分配器は以上のように構成し
ているので、各細管から流出する液相流体の流量が均等
な気液二相流体の分配器が従来のような回転翼なしで得
られるという効果がある。[Effects of the Invention] Since the gas-liquid two-phase fluid distributor of the present invention is configured as described above, the gas-liquid two-phase fluid distributor in which the flow rate of the liquid phase fluid flowing out from each capillary is equal is different from the conventional gas-liquid two-phase fluid distributor. This has the advantage that it can be obtained without the need for rotary blades.
第1図はこの発明の気液二相流体の分配器の垂直断面図
、第2図は第1図の■−■断面図、第3図はこの発明の
他の実施例を示す垂直断面図、第4図は従来の気液二相
流体の分配器の垂直断面図である。
なお図中(1)は分配管、(2)は細管、(4)は気液
二相流体である。
第
3
図
介へ4
手
続
補
正
書
(自
発)
6、補
正
の
内
容
平成
2年
5月23日
(1)
明細書第4頁第7行を次の通り訂正する。Fig. 1 is a vertical cross-sectional view of a gas-liquid two-phase fluid distributor of the present invention, Fig. 2 is a cross-sectional view taken along the line ■-■ of Fig. 1, and Fig. 3 is a vertical cross-sectional view showing another embodiment of the present invention. , FIG. 4 is a vertical cross-sectional view of a conventional gas-liquid two-phase fluid distributor. In the figure, (1) is a distribution pipe, (2) is a thin tube, and (4) is a gas-liquid two-phase fluid. To Figure 3 4 Procedural amendment (voluntary) 6. Contents of amendment May 23, 1990 (1) Line 7 of page 4 of the specification is corrected as follows.
Claims (1)
複数の分流用細管を植立させた分配器において、上記分
配管の内径を上記流体の流れ方向に縮径させて各細管か
らの流出液流量を均一化するようにしたことを特徴とす
る気液二相流体の分配器。In a distributor in which a plurality of dividing thin tubes with the same flow path resistance are installed in a distribution pipe through which a gas-liquid two-phase fluid passes, the inner diameter of the distribution pipe is reduced in the flow direction of the fluid, and each A gas-liquid two-phase fluid distributor characterized in that the flow rate of liquid flowing out from a thin tube is made uniform.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2055085A JP2767963B2 (en) | 1990-03-08 | 1990-03-08 | Gas-liquid two-phase fluid distributor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2055085A JP2767963B2 (en) | 1990-03-08 | 1990-03-08 | Gas-liquid two-phase fluid distributor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03260567A true JPH03260567A (en) | 1991-11-20 |
JP2767963B2 JP2767963B2 (en) | 1998-06-25 |
Family
ID=12988883
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2055085A Expired - Lifetime JP2767963B2 (en) | 1990-03-08 | 1990-03-08 | Gas-liquid two-phase fluid distributor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2767963B2 (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5901785A (en) * | 1996-03-29 | 1999-05-11 | Sanden Corporation | Heat exchanger with a distribution device capable of uniformly distributing a medium to a plurality of exchanger tubes |
US5934367A (en) * | 1996-12-19 | 1999-08-10 | Sanden Corporation | Heat exchanger |
US5979547A (en) * | 1996-03-22 | 1999-11-09 | Sanden Corporation | Distribution device capable of uniformly distributing a medium to a plurality of tubes of a heat exchanger |
US6814136B2 (en) | 2002-08-06 | 2004-11-09 | Visteon Global Technologies, Inc. | Perforated tube flow distributor |
JP2011017505A (en) * | 2009-07-10 | 2011-01-27 | Mitsubishi Electric Corp | Refrigerant distributor and heat pump device |
JP2012207912A (en) * | 2012-06-28 | 2012-10-25 | Mitsubishi Electric Corp | Refrigerant distributor and heat pump device |
US8302673B2 (en) * | 2004-11-12 | 2012-11-06 | Carrier Corporation | Parallel flow evaporator with spiral inlet manifold |
JP2013002688A (en) * | 2011-06-14 | 2013-01-07 | Sharp Corp | Parallel flow type heat exchanger and air conditioner with the same |
CN104764256A (en) * | 2015-03-31 | 2015-07-08 | 广东美的暖通设备有限公司 | Heat exchanger and multi-split system with the same |
CN107270454A (en) * | 2017-08-03 | 2017-10-20 | 吴喜平 | Catch basin flow equalizing low-resistance power air diffuser |
JP2018044759A (en) * | 2017-06-05 | 2018-03-22 | 三菱電機株式会社 | Header and air conditioner |
EP3306232A1 (en) * | 2016-10-05 | 2018-04-11 | Mitsubishi Heavy Industries Thermal Systems, Ltd. | Evaporator and refrigerant circuit |
DE102005059920B4 (en) * | 2005-12-13 | 2019-07-04 | Mahle International Gmbh | Heat exchanger, in particular evaporator |
WO2019224978A1 (en) * | 2018-05-24 | 2019-11-28 | 三菱電機株式会社 | Shell-and-tube heat exchanger |
CN114413529A (en) * | 2022-04-02 | 2022-04-29 | 山东中科万隆电声科技有限公司 | Refrigerant distributor |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50127948U (en) * | 1974-04-05 | 1975-10-21 | ||
JPH0331665A (en) * | 1989-06-28 | 1991-02-12 | Matsushita Electric Ind Co Ltd | Flow diverter |
-
1990
- 1990-03-08 JP JP2055085A patent/JP2767963B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50127948U (en) * | 1974-04-05 | 1975-10-21 | ||
JPH0331665A (en) * | 1989-06-28 | 1991-02-12 | Matsushita Electric Ind Co Ltd | Flow diverter |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5979547A (en) * | 1996-03-22 | 1999-11-09 | Sanden Corporation | Distribution device capable of uniformly distributing a medium to a plurality of tubes of a heat exchanger |
US5901785A (en) * | 1996-03-29 | 1999-05-11 | Sanden Corporation | Heat exchanger with a distribution device capable of uniformly distributing a medium to a plurality of exchanger tubes |
US5934367A (en) * | 1996-12-19 | 1999-08-10 | Sanden Corporation | Heat exchanger |
US6814136B2 (en) | 2002-08-06 | 2004-11-09 | Visteon Global Technologies, Inc. | Perforated tube flow distributor |
US8302673B2 (en) * | 2004-11-12 | 2012-11-06 | Carrier Corporation | Parallel flow evaporator with spiral inlet manifold |
DE102005059920B4 (en) * | 2005-12-13 | 2019-07-04 | Mahle International Gmbh | Heat exchanger, in particular evaporator |
JP2011017505A (en) * | 2009-07-10 | 2011-01-27 | Mitsubishi Electric Corp | Refrigerant distributor and heat pump device |
JP2013002688A (en) * | 2011-06-14 | 2013-01-07 | Sharp Corp | Parallel flow type heat exchanger and air conditioner with the same |
JP2012207912A (en) * | 2012-06-28 | 2012-10-25 | Mitsubishi Electric Corp | Refrigerant distributor and heat pump device |
CN104764256A (en) * | 2015-03-31 | 2015-07-08 | 广东美的暖通设备有限公司 | Heat exchanger and multi-split system with the same |
US20180010857A1 (en) * | 2015-03-31 | 2018-01-11 | Gd Midea Heating & Ventilating Equipment Co., Ltd. | Heat exchanger and multi-split system having same |
WO2016155367A1 (en) * | 2015-03-31 | 2016-10-06 | 广东美的暖通设备有限公司 | Heat exchanger and multi-split system having same |
EP3306232A1 (en) * | 2016-10-05 | 2018-04-11 | Mitsubishi Heavy Industries Thermal Systems, Ltd. | Evaporator and refrigerant circuit |
JP2018044759A (en) * | 2017-06-05 | 2018-03-22 | 三菱電機株式会社 | Header and air conditioner |
CN107270454A (en) * | 2017-08-03 | 2017-10-20 | 吴喜平 | Catch basin flow equalizing low-resistance power air diffuser |
WO2019224978A1 (en) * | 2018-05-24 | 2019-11-28 | 三菱電機株式会社 | Shell-and-tube heat exchanger |
JPWO2019224978A1 (en) * | 2018-05-24 | 2021-04-01 | 三菱電機株式会社 | Shell and tube heat exchanger |
CN114413529A (en) * | 2022-04-02 | 2022-04-29 | 山东中科万隆电声科技有限公司 | Refrigerant distributor |
CN114413529B (en) * | 2022-04-02 | 2022-06-28 | 山东中科万隆电声科技有限公司 | Refrigerant distributor |
Also Published As
Publication number | Publication date |
---|---|
JP2767963B2 (en) | 1998-06-25 |
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