JP2557497Y2 - Heat exchanger shunt - Google Patents
Heat exchanger shuntInfo
- Publication number
- JP2557497Y2 JP2557497Y2 JP1991084825U JP8482591U JP2557497Y2 JP 2557497 Y2 JP2557497 Y2 JP 2557497Y2 JP 1991084825 U JP1991084825 U JP 1991084825U JP 8482591 U JP8482591 U JP 8482591U JP 2557497 Y2 JP2557497 Y2 JP 2557497Y2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- pipe
- circular
- section
- heat exchanger
- 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)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Description
【0001】[0001]
【産業上の利用分野】本考案はエバポレータとして用い
られる空調用熱交換器の分流器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a shunt of an air conditioner heat exchanger used as an evaporator.
【0002】[0002]
【従来の技術】空調用熱交換器は、コンパクトで高性能
化が求められている。そこで、熱交換器コアに用いられ
るチューブを細く且つより多く使用する傾向が高まって
いる。このように細い多数の管を使用する場合には、冷
媒の入口パイプから分流器を介して複数のチューブに同
時にその冷媒を供給するように構成する。この分流器は
一般に鋳造後、切削加工を行ったものを用いていた。こ
のような鋳物部品からなる分流器は、その製作工数が多
くコスト高となる欠点がある。さらに、その鋳物製分流
器は、それに接続される出入口パイプに比べて肉厚が厚
くならざるを得ず、パイプろう付けの際の熱容量に大き
な差が生じ、ろう付け不良を起こし易い欠点があった。
そこで、パイプ材を塑性変形してこの分流器を製作する
ことも考えられるが、この場合には各流路に均一に冷媒
の分流が起こり難い欠点がある。2. Description of the Related Art Heat exchangers for air conditioning are required to be compact and have high performance. Therefore, there is an increasing tendency to use thinner and more tubes used for the heat exchanger core. When a large number of thin tubes are used, the refrigerant is simultaneously supplied to a plurality of tubes from a refrigerant inlet pipe via a flow divider. In general, the current divider used was one that had been subjected to cutting after casting. The flow divider composed of such a cast component has a drawback that the number of manufacturing steps is large and the cost is high. Furthermore, the cast distributor has to be thicker than the inlet and outlet pipes connected to it, resulting in a large difference in heat capacity at the time of brazing the pipe, and has a disadvantage that brazing failure is liable to occur. Was.
Therefore, it is conceivable to manufacture this flow divider by plastically deforming the pipe material. However, in this case, there is a disadvantage that the flow of the refrigerant is hardly uniformly distributed in each flow path.
【0003】[0003]
【課題を解決するための手段】そこで本考案は、上記の
問題点を解決するため次の構成をとる。本考案の熱交換
器の分流器は、気体と液体とに相変化する冷媒が流通す
るチューブの分流部に配置されるものにおいて、一本の
パイプ材が塑性変形されてその一端部に一つの断面円形
な入口管部1が設けられる。そしてその入口管部1に一
体的に偏平管部2が連設され、その偏平管部2の先端部
に断面を眼鏡状に形成した複数の円形管部3,3が偏平
管部2の断面の長軸方向に並列される。そして、円形管
部3,3の境の延長線上で偏平管部2に部分的に断面が
眼鏡状のくびれとなる誘導部4が形成され、その誘導部
4と円形管部3との間に、その誘導部より分岐して導か
れた連通部5が形成され、その連通部5により冷媒が互
いに連通するように構成したことを特徴とする。Accordingly, the present invention employs the following structure to solve the above-mentioned problems. The flow divider of the heat exchanger of the present invention is arranged at the branch of a tube through which a refrigerant that changes phase into gas and liquid flows, and one pipe material is plastically deformed and one end is provided at one end thereof. An inlet pipe 1 having a circular cross section is provided. A flat tube portion 2 is integrally connected to the inlet tube portion 1, and a plurality of circular tube portions 3, 3, each having a cross-sectional shape formed in a spectacle shape, are formed at the tip of the flat tube portion 2. Are arranged in parallel in the long axis direction. Then, on the extension of the boundary between the circular pipes 3, 3, a guide 4 having a spectacle-shaped constriction is formed partially in the flat pipe 2, and between the guide 4 and the circular pipe 3. A communication portion 5 branched from the guide portion is formed, and the communication portion 5 allows the refrigerant to communicate with each other.
【0004】[0004]
【作用】本考案の分流器によれば、入口管部1から流入
した冷媒は図1に示す如く夫々の誘導部4に整流されて
各円形管部3,3に導かれる。しかもこの円形管部3と
誘導部4との間に形成された連通部5の存在により、複
数の円形管部3,3に夫々導かれる冷媒12の圧力が互い
に均一化し、各円形管部3に流通する冷媒が均一に分流
する。そして、図3の如く夫々の円形管部3に接続され
た出口パイプ8に冷媒が導かれ、チューブ7とフィン14
とからなる熱交換器コア6の各部に分配され、熱交換器
各部の冷却能力を均一に保持する。According to the flow divider of the present invention, the refrigerant flowing from the inlet pipe 1 is rectified by the respective guides 4 and guided to the respective circular pipes 3, 3 as shown in FIG. In addition, the presence of the communication portion 5 formed between the circular tube portion 3 and the guide portion 4 makes the pressure of the refrigerant 12 guided to the plurality of circular tube portions 3 and 3 uniform with each other. The refrigerant circulating in the air is distributed uniformly. Then, as shown in FIG. 3, the refrigerant is led to the outlet pipes 8 connected to the respective circular pipe sections 3, and
The cooling capacity of each part of the heat exchanger 6 is uniformly maintained.
【0005】[0005]
【実施例】次に図面に基づいて本考案の実施例につき説
明する。図1は本考案の分流器の使用状態を示す縦断面
図であり、図2は同分流器の斜視略図、図3は同分流器
と熱交換器コアとの接続状態示す説明図、図4は本考案
の第二実施例の分流器の斜視略図である。第一実施例の
分流器は、図1〜図2に示す如く一本の円形パイプを塑
性加工することにより製作される。即ち、その一端部に
断面円形の入口管部1を形成すると共に、中間部及び他
端部を偏平に形成し且つ、断続的に偏平部の両側から押
圧し断面眼鏡状に形成する。そして、分流器13の他端部
に一対の円形管部3,3を形成する。このような分流器
13は、入口管部1を除き偏平管部2の軸線上において対
向する内面が断続的に誘導部4により圧着されると共
に、一対の円形管部3,3間も同様に圧着されている。
そしてこの円形管部3は、横断面が等しく形成されてい
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a longitudinal sectional view showing a use state of the current splitter of the present invention, FIG. 2 is a schematic perspective view of the current splitter, FIG. 3 is an explanatory view showing a connection state between the current splitter and a heat exchanger core, and FIG. FIG. 4 is a schematic perspective view of a flow divider according to a second embodiment of the present invention. The flow divider of the first embodiment is manufactured by plastically processing a single circular pipe as shown in FIGS. That is, the inlet pipe part 1 having a circular cross section is formed at one end thereof, and the intermediate part and the other end are formed flat and intermittently pressed from both sides of the flat part to form eyeglasses in cross section. Then, a pair of circular pipes 3 and 3 are formed at the other end of the flow divider 13. Such a shunt
In 13, the inner surfaces of the flat tube portion 2 facing each other on the axis except the inlet tube portion 1 are intermittently crimped by the guide portion 4, and the pair of circular tube portions 3 and 3 are similarly crimped.
And this circular pipe | tube part 3 is formed in cross section equally.
【0006】このようにしてなる分流器13の入口管部1
に入口パイプ9が嵌入し、その嵌入部がろう付け又はハ
ンダ付け固定される。又、一対の円形管部3には夫々出
口パイプ8の端部が嵌入し、その嵌入部がろう付け又は
ハンダ付け固定される。そして夫々の出口パイプ8の他
端部が図3に示す如く熱交換器コア6のチューブ7の端
部に液密に接合される。このチューブ7は多数のフィン
14のチューブ挿通孔に挿通され、該挿通部が熱的に接合
されている。なお、このチューブ7は気液二相状態の冷
媒の流通路となり、一般には多数のチューブ7の端部ど
うしが図示しないUベンド管で接合され、冷媒がそれら
を蛇行状に流通するものである。そして、チューブ7外
面及びフィン14外面に流通する空気流を冷却するもので
ある。[0006] The inlet pipe 1 of the flow divider 13 thus constructed.
The inlet pipe 9 is fitted into the fitting, and the fitted portion is fixed by brazing or soldering. The ends of the outlet pipes 8 are fitted into the pair of circular pipes 3, respectively, and the fitted portions are fixed by brazing or soldering. The other end of each outlet pipe 8 is liquid-tightly joined to the end of the tube 7 of the heat exchanger core 6 as shown in FIG. This tube 7 has many fins
Fourteen tube insertion holes are inserted, and the insertion part is thermally joined. The tube 7 serves as a flow path for a refrigerant in a gas-liquid two-phase state. Generally, ends of a large number of tubes 7 are joined by a U-bend tube (not shown), and the refrigerant flows in a meandering manner. . Then, it cools the airflow flowing through the outer surface of the tube 7 and the outer surface of the fin 14.
【0007】次に図4は本考案の第二実施例であり、こ
の実施例では三つの円形管部3が分流器13の一端部に形
成されている。そして、夫々の円形管部3の境目の延長
線上に断続的に誘導部4が設けられる。その誘導部4と
円形管部3の境目との間に連通部5が形成されている。
なお、各実施例において誘導部4の長さ及び連通部5の
長さは適宜選択される。この誘導部4は各円形管部3に
冷媒を導くための整流効果が得られる程度とし、連通部
5は夫々の分流路内の冷媒圧力を均一にする程度に設計
される。なお分流器13の材質は、入口パイプ9及び出口
パイプ8と同一のもの又はそれに近い材料を選択するこ
とが好ましい。入口パイプ9及び出口パイプ8は、銅管
又はアルミニューム管或いは黄銅管が採用されている。FIG. 4 shows a second embodiment of the present invention. In this embodiment, three circular tubes 3 are formed at one end of the flow divider 13. The guides 4 are provided intermittently on the extension of the boundary between the respective circular pipes 3. A communication portion 5 is formed between the guide portion 4 and a boundary between the circular tube portions 3.
In each embodiment, the length of the guiding portion 4 and the length of the communicating portion 5 are appropriately selected. The guide section 4 is designed to have a rectifying effect for guiding the refrigerant to each of the circular pipe sections 3, and the communication section 5 is designed to make the refrigerant pressure in each branch channel uniform. It is preferable to select the same material as the inlet pipe 9 and the outlet pipe 8 or a material similar thereto as the material of the flow divider 13. As the inlet pipe 9 and the outlet pipe 8, a copper pipe, an aluminum pipe, or a brass pipe is adopted.
【0008】[0008]
【考案の効果】本考案の分流器は以上のように構成した
から、入口管部から流入した冷媒は夫々の円形管部に向
かって誘導部4により誘導され、整流して円滑に導かれ
ると共に、その誘導部と円形管部との間に存在する連通
部の存在により、各部に導かれる冷媒圧力が均一とな
り、冷媒の分流を均一に行うことができ、それにより下
流側に配置される熱交換器の効率を向上させ得る。即
ち、熱交換器各部における伝熱性を均一化し、熱交換性
能を向上させ得る。しかも、この分流器は一本のパイプ
材が塑性加工されて作られたものであるから、その分流
器に接続される出入口パイプとのろう付け性が良好とな
る。なぜならば分流器とパイプとの熱容量の差が従来の
切削加工品に比べて小さいため、熱容量の差に基づくろ
う付け不良がなくなる。又、加工が容易で軽量化に寄与
できる。The flow divider according to the present invention is constructed as described above, so that the refrigerant flowing from the inlet pipes is guided by the guides 4 toward the respective circular pipes, and is rectified and guided smoothly. Due to the existence of the communicating portion existing between the guide portion and the circular tube portion, the pressure of the refrigerant guided to each portion becomes uniform, and the refrigerant can be uniformly diverted. The efficiency of the exchanger can be improved. That is, the heat transfer in each part of the heat exchanger can be made uniform, and the heat exchange performance can be improved. In addition, since the flow distributor is formed by plastically processing a single pipe material, the brazing performance with the inlet / outlet pipe connected to the flow distributor is improved. This is because the difference in heat capacity between the flow divider and the pipe is smaller than that of a conventional machined product, so that brazing failure based on the difference in heat capacity is eliminated. In addition, processing is easy, which can contribute to weight reduction.
【図1】本考案の第一実施例の分流器の使用状態を示す
縦断面図。FIG. 1 is a longitudinal sectional view showing a use state of a flow divider according to a first embodiment of the present invention.
【図2】第一実施例の分流器の斜視略図。FIG. 2 is a schematic perspective view of the flow divider of the first embodiment.
【図3】第一実施例の分流器の使用状態を示す一部縦断
面説明図。FIG. 3 is a partial longitudinal sectional explanatory view showing a use state of the flow divider of the first embodiment.
【図4】本考案の第二実施例の分流器の斜視略図。FIG. 4 is a schematic perspective view of a flow divider according to a second embodiment of the present invention.
【図5】従来型分流器の縦断面図。FIG. 5 is a longitudinal sectional view of a conventional flow divider.
【図6】従来型分流器の側面図。FIG. 6 is a side view of a conventional flow divider.
1 入口管部 2 偏平管部 3 円形管部 4 誘導部 5 連通部 6 熱交換器コア 7 チューブ 8 出口パイプ 9 入口パイプ 11 サイドメンバ 12 冷媒 13 分流器 14 フィン DESCRIPTION OF SYMBOLS 1 Inlet pipe part 2 Flat pipe part 3 Circular pipe part 4 Guide part 5 Communication part 6 Heat exchanger core 7 Tube 8 Outlet pipe 9 Inlet pipe 11 Side member 12 Refrigerant 13 Divider 14 Fin
Claims (1)
るチューブの分流部に配置される熱交換器の分流器にお
いて、一本のパイプ材が塑性加工されて、その一端部に
一つの断面円形な入口管部(1)が設けられ、その入口
管部(1)に一体的に偏平管部(2)が連設され、その
偏平管部(2)先端部に断面が眼鏡状に変形された複数
の円形管部(3)(3)が前記偏平管部(2)の断面の
長手方向に並列され、前記円形管部(3)(3)の境の
延長線上で前記偏平管部(2)に部分的に断面が眼鏡状
のくびれとなる誘導部(4)が形成され、その誘導部
(4)と前記円形管部(3)との間に、その誘導部によ
り分岐して導かれた夫々の前記冷媒が互いに連通する連
通部(5)が形成されたことを特徴とする熱交換器の分
流器。In a flow divider of a heat exchanger disposed at a branch of a tube through which a refrigerant that changes phase into a gas and a liquid flows, one pipe member is plastically processed, and one pipe member is provided at one end thereof. An inlet tube (1) having a circular cross section is provided, a flat tube (2) is integrally connected to the inlet tube (1), and the cross section of the flat tube (2) has a spectacle shape at the tip. A plurality of deformed circular pipe sections (3) and (3) are arranged in parallel in the longitudinal direction of the cross section of the flat pipe section (2), and the flat pipe section extends along a boundary between the circular pipe sections (3) and (3). A guiding portion (4) having a spectacle-shaped constriction is formed partially in the portion (2), and is branched by the guiding portion between the guiding portion (4) and the circular tube portion (3). A flow divider for a heat exchanger, wherein a communication part (5) is formed in which the respective refrigerants guided by the flow are communicated with each other.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1991084825U JP2557497Y2 (en) | 1991-09-20 | 1991-09-20 | Heat exchanger shunt |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1991084825U JP2557497Y2 (en) | 1991-09-20 | 1991-09-20 | Heat exchanger shunt |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0527567U JPH0527567U (en) | 1993-04-09 |
JP2557497Y2 true JP2557497Y2 (en) | 1997-12-10 |
Family
ID=13841540
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1991084825U Expired - Lifetime JP2557497Y2 (en) | 1991-09-20 | 1991-09-20 | Heat exchanger shunt |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2557497Y2 (en) |
-
1991
- 1991-09-20 JP JP1991084825U patent/JP2557497Y2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0527567U (en) | 1993-04-09 |
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