JPH02197769A - Flow divider - Google Patents
Flow dividerInfo
- Publication number
- JPH02197769A JPH02197769A JP1018113A JP1811389A JPH02197769A JP H02197769 A JPH02197769 A JP H02197769A JP 1018113 A JP1018113 A JP 1018113A JP 1811389 A JP1811389 A JP 1811389A JP H02197769 A JPH02197769 A JP H02197769A
- Authority
- JP
- Japan
- Prior art keywords
- inflow pipe
- flow
- refrigerant
- collision
- joined
- 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
Links
- 239000003507 refrigerant Substances 0.000 abstract description 17
- 239000007788 liquid Substances 0.000 abstract description 15
- 230000000694 effects Effects 0.000 abstract description 6
- 230000005514 two-phase flow Effects 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract 1
- 239000012071 phase Substances 0.000 description 8
- 239000007791 liquid phase Substances 0.000 description 6
- 238000005057 refrigeration Methods 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は空調機器や冷凍機器の冷凍サイクルにおいて冷
媒を均等に分流するだめ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 uniformly dividing a refrigerant in a refrigeration cycle of an air conditioner or a refrigerator.
従来の技術
近年、冷凍システムのマルチ化、及び熱交換器の伝熱管
細径化に伴う複数回路化等に対応するために分流器が多
用され、その重要度が増している。BACKGROUND OF THE INVENTION In recent years, flow dividers have been frequently used to cope with the multiplication of refrigeration systems and the creation of multiple circuits due to the reduction in diameter of heat exchanger tubes in heat exchangers, and their importance has been increasing.
以下、図面を参照しながら従来の分流器について説明を
行う。Hereinafter, a conventional flow divider will be explained with reference to the drawings.
第4図は従来の分流器の形状を示し、第6図は分流器内
部の冷媒状態を示す。FIG. 4 shows the shape of a conventional flow divider, and FIG. 6 shows the state of the refrigerant inside the flow divider.
第5図、第6図において、1は分流器であシ円筒状容器
2と、円筒状容器2の片端に接続される流入管3と、他
端に接続される複数の流出管4とから構成される。In FIGS. 5 and 6, 1 is a flow divider which is connected to a cylindrical container 2, an inflow pipe 3 connected to one end of the cylindrical container 2, and a plurality of outflow pipes 4 connected to the other end. configured.
以上のように構成される分流器について第5図を用いて
その動作を説明する。The operation of the flow divider constructed as described above will be explained using FIG. 5.
分流器1において、流入管3から円筒状容器2へ流入す
る冷媒は、気相6と液相6との気液二相の状態となって
いる。この冷媒は複数の流出管4へ分配されながら、分
流器1を通過するが液相6の一部は円筒状容器2の上部
壁面に衝突、落下し、円筒状容器2の下部で滞留、循環
し液溜シを形成する。同様に気相6の一部は円筒状容器
2の上部で滞留循環し気溜りを形成する。In the flow divider 1, the refrigerant flowing into the cylindrical container 2 from the inflow pipe 3 is in a gas-liquid two-phase state of a gas phase 6 and a liquid phase 6. This refrigerant passes through the flow divider 1 while being distributed to a plurality of outflow pipes 4, but a part of the liquid phase 6 collides with the upper wall surface of the cylindrical container 2, falls, stays in the lower part of the cylindrical container 2, and circulates. A liquid reservoir is formed. Similarly, a part of the gas phase 6 is retained and circulated in the upper part of the cylindrical container 2 to form an air pocket.
発明が解決しようとする課題
しかしながら上記構成では、冷媒の流れは液溜りの液面
を流入する二相流によりかく乱すると同時に、同伴する
液相θの量が不均一になるだけでなく、例えば分流器1
が傾斜した場合には、液面が、複数の流出管4のいずれ
かに近づく等により、各流出管4への分流は、非常に不
安定な要素が大きいという課題を有していた。Problems to be Solved by the Invention However, with the above configuration, the flow of the refrigerant is disturbed by the incoming two-phase flow on the liquid surface of the liquid reservoir, and at the same time, the amount of the accompanying liquid phase θ becomes uneven, and, for example, the flow of the refrigerant becomes uneven. Vessel 1
In the case where the liquid level is inclined, the liquid level approaches one of the plurality of outflow pipes 4, so that the branching of the flow to each outflow pipe 4 has a large unstable factor.
また、円管状容器2は複数の流出管4を接続する為、必
然的に大型化、高コスト化するだけでなく、接合箇所も
多い為、もれに対する信頼性の而でも課題を有していた
。Furthermore, since the tubular container 2 connects a plurality of outflow pipes 4, it not only inevitably becomes larger and more expensive, but also has many joints, which poses problems in terms of reliability against leakage. Ta.
本発明は上記課題を解決するもので、均等で安定した分
流が行え、しかも、小型、低コストで、もれに対する信
頼性の高い分流器を提供するものである。The present invention solves the above problems and provides a flow divider that can perform uniform and stable flow division, is small in size, is low in cost, and has high reliability against leakage.
課題を解決するための手段
上記課題を解決するために本発明の分流器は、流入管と
、流入管内の流れを略直角方向に変更する流入管先端に
接合された衝突壁と、流入管壁面に放射状に接合された
複数の流出管とから構成されたものである。Means for Solving the Problems In order to solve the above problems, the flow divider of the present invention includes an inflow pipe, a collision wall joined to the tip of the inflow pipe that changes the flow in the inflow pipe in a substantially perpendicular direction, and an inflow pipe wall surface. It is composed of a plurality of outflow pipes connected radially to the outflow pipe.
作 用
本発明は上記した構成によって、流入管を流れる冷媒の
流れを、衝突壁に衝突させて、気相9gI相の混合を進
め、液溜り、気溜りの発生する内容積部分を廃除した事
によυ、放射状に接合された流出管へ円滑に流出させる
ことによって均等に分流を行う事ができる。また、流出
管を流入管に放射状に直接接合するだめ、従来の円筒状
容器が不要となり、小型、低コストでもれに対する信頼
性も高いものとなる。Effect: With the above-described configuration, the present invention causes the flow of refrigerant flowing through the inflow pipe to collide with the collision wall to advance the mixing of the gas phase 9gI phase and eliminate the internal volume portion where liquid pools and gas pools occur. Therefore, it is possible to divide the flow evenly by allowing the flow to flow smoothly into the radially connected outflow pipes. Furthermore, since the outflow pipe is directly joined to the inflow pipe in a radial manner, the conventional cylindrical container is not required, and the system is small, low cost, and highly reliable against leakage.
実施例
以下本発明の実施例の分流器について図面を参照しなが
ら説明する。EMBODIMENTS Below, flow dividers according to embodiments of the present invention will be described with reference to the drawings.
第1図は本発明の第1の実施例における分流器の外観を
示すもので、第2図はその断面図を示す。FIG. 1 shows the appearance of a flow divider according to a first embodiment of the present invention, and FIG. 2 shows its sectional view.
また第3図は本発明の第2の実施例を示すもので、第4
図はその断面図を示す。第1図から第4図において、1
1.11’は分流器を示し、12.1ノは流入管、13
、13’は流入管先端に接合された衝突壁、14 、
14’は流入管壁面に放射状に接合された複数の流出管
である。Further, FIG. 3 shows a second embodiment of the present invention, and a fourth embodiment of the present invention is shown in FIG.
The figure shows its cross-sectional view. In Figures 1 to 4, 1
1.11' indicates the flow divider, 12.1 indicates the inflow pipe, 13
, 13' is a collision wall joined to the tip of the inflow pipe, 14,
Reference numeral 14' denotes a plurality of outflow pipes radially joined to the wall surface of the inflow pipe.
以上のように構成された分流器11 、11’について
以下その動作について説明する。The operation of the flow dividers 11 and 11' configured as described above will be explained below.
第1の実施例、第2の実施例ともその動作は同様であシ
第1の実施例の第2図を用いて説明する。The operation of the first embodiment and the second embodiment is similar, and will be explained using FIG. 2 of the first embodiment.
流入管12を流れる冷媒は、気相16と液相16との二
相流の状1叫で流出管14へと分流して出ていく。この
時、流入管12内では不均一であった前記二相流の冷媒
は衝突壁13に衝突することにより混合され、気相15
と液相16との混合状態が均一化される。均一化された
冷媒は衝突壁13に沿って放射状に広がり流入管壁面に
放射状に接合された流出管14へ分流される。この時分
流部分に液溜り、気溜りの形成される容積部分がないた
め、冷媒の気液混合状態は衝突による混合効果で均一化
されたままであり、それ故均等に分流されることになる
。The refrigerant flowing through the inflow pipe 12 is divided into the outflow pipe 14 in a two-phase flow of a gas phase 16 and a liquid phase 16 and exits. At this time, the refrigerant in the two-phase flow, which was non-uniform in the inflow pipe 12, collides with the collision wall 13 and is mixed, and the gas phase 15
The mixing state of the liquid phase 16 and the liquid phase 16 is made uniform. The homogenized refrigerant spreads radially along the collision wall 13 and is divided into an outflow pipe 14 radially joined to the wall surface of the inflow pipe. At this time, since there is no volumetric area in which liquid pools or gas pools are formed in the divided flow portion, the gas-liquid mixing state of the refrigerant remains uniform due to the mixing effect due to the collision, and therefore the refrigerant is evenly divided.
また、流出管を放射状に直接流入管へ接続した構成をも
つため、従来の分流器に対して小型化。In addition, because the outflow pipe is connected radially directly to the inflow pipe, it is more compact than conventional flow dividers.
低コスト化が可能であり、接合箇所が少ないため、もれ
に対する信頼性も高いものとなる。特に第2の実施例で
は大幅な小型化が可能となる。Cost reduction is possible, and since there are few joints, reliability against leakage is also high. In particular, the second embodiment allows for significant downsizing.
以上のように本実施例によれば、流入管と流入管内の流
れを略直角方向に変更する流入管先端に接合された衝突
壁と、流入管壁面に放射状に接合された複数の流出管と
から構成したことにより均等な分流を実現すると同時に
小型化、低コスト化を実現すると共にもれに対する信頼
性も高めることができる。As described above, according to this embodiment, the inflow pipe and the collision wall joined to the tip of the inflow pipe that changes the flow inside the inflow pipe in a substantially perpendicular direction, and the plurality of outflow pipes joined radially to the wall surface of the inflow pipe. By configuring this structure, it is possible to achieve uniform flow division, downsizing, and cost reduction, as well as improving reliability against leakage.
尚、本実施例では衝突壁を平面形としたが、半円形でも
同様の効果が得られる。また、絞り加工等による一体形
状でも同様の効果が得られる。In this embodiment, the collision wall has a planar shape, but the same effect can be obtained even if it is semicircular. Further, the same effect can be obtained by using an integral shape by drawing or the like.
発明の効果
以上のように本発明は流入管と、流入管内の流れを略直
角方向に変更する流入管先端に接合された衝突壁と、流
入管側面に放射上に接合された複数の流出管とから構成
したことにより、衝突による気液二相の混合を行い、気
溜りや液溜りがなくなり均等な分流を実現できるもので
ある。また、小型化、低コスト化が可能であり、もれに
対する信頼性も高いものである。Effects of the Invention As described above, the present invention includes an inflow pipe, a collision wall joined to the tip of the inflow pipe for changing the flow inside the inflow pipe in a substantially perpendicular direction, and a plurality of outflow pipes joined radially to the side surface of the inflow pipe. With this structure, gas-liquid two-phase mixing occurs through collision, eliminating air and liquid pools and achieving uniform flow separation. Further, it is possible to reduce the size and cost, and has high reliability against leakage.
第1図は本発明の第1の実施例における分流器の外観図
、第2図は第1図の断面図、第3図は本発明の第2の実
施例における外観図、第4図は第3図の断面図、第6図
は従来の分流器の外観図、第6図は第5図の断面図であ
る。
11・・・・・・分流器、12・・・・・・流入管、1
3・・・・・・衝突壁、14・・・・・・流出管。
代理人の氏名 弁理士 粟 野 重 孝 ほか1名簿
図
第
図Fig. 1 is an external view of a flow divider according to a first embodiment of the present invention, Fig. 2 is a sectional view of Fig. 1, Fig. 3 is an external view of a flow divider according to a second embodiment of the present invention, and Fig. 4 is an external view of a flow divider according to a first embodiment of the present invention. FIG. 3 is a sectional view, FIG. 6 is an external view of a conventional flow divider, and FIG. 6 is a sectional view of FIG. 5. 11... Flow divider, 12... Inflow pipe, 1
3... Collision wall, 14... Outflow pipe. Name of agent: Patent attorney Shigetaka Awano and 1 other list
Claims (1)
に配設された衝突壁と、流入管壁面に放射状に接合され
た複数の流出管とから構成される分流器。A flow divider consisting of an inflow pipe, a collision wall disposed at the tip of the inflow pipe that changes the direction of flow within the inflow pipe, and a plurality of outflow pipes radially joined to the wall surface of the inflow pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1018113A JPH02197769A (en) | 1989-01-27 | 1989-01-27 | Flow divider |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1018113A JPH02197769A (en) | 1989-01-27 | 1989-01-27 | Flow divider |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02197769A true JPH02197769A (en) | 1990-08-06 |
Family
ID=11962561
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1018113A Pending JPH02197769A (en) | 1989-01-27 | 1989-01-27 | Flow divider |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02197769A (en) |
-
1989
- 1989-01-27 JP JP1018113A patent/JPH02197769A/en active Pending
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