JPH03251690A - Lamination type heat exchanger - Google Patents
Lamination type heat exchangerInfo
- Publication number
- JPH03251690A JPH03251690A JP4762290A JP4762290A JPH03251690A JP H03251690 A JPH03251690 A JP H03251690A JP 4762290 A JP4762290 A JP 4762290A JP 4762290 A JP4762290 A JP 4762290A JP H03251690 A JPH03251690 A JP H03251690A
- Authority
- JP
- Japan
- Prior art keywords
- fluid
- header
- space
- grooves
- inlet pipe
- 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
- 238000003475 lamination Methods 0.000 title 1
- 239000012530 fluid Substances 0.000 claims abstract description 38
- 238000004378 air conditioning Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
Landscapes
- Details Of Heat-Exchange And Heat-Transfer (AREA)
- 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
本発明は空調システム等に用いられる層積式熱交換器に
関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a stacked heat exchanger used in air conditioning systems and the like.
従来の技術
積層式熱交換器は、空調システム等においてフロンとフ
ロンあるいはフロンと水、水と水との間で熱交換するの
に用いられ、近年、空調システムの多様化に伴い、その
需要が高まってきている。Conventional technology Laminated heat exchangers are used to exchange heat between fluorocarbons, fluorocarbons and water, or water and water in air conditioning systems, etc. In recent years, with the diversification of air conditioning systems, the demand for them has increased. It's increasing.
以下第5図から第8図とともに従来例(%開昭60−2
53794号公報)について説明する。Below, along with Figures 5 to 8, the conventional example (%
53794) will be explained.
第5図は従来の積層式熱交換器の斜視図、第6図は熱交
換板の斜視図、第7図は第5図のB −B断面図、第8
図は第5図のC−C断面図である。Fig. 5 is a perspective view of a conventional stacked heat exchanger, Fig. 6 is a perspective view of a heat exchange plate, Fig. 7 is a sectional view taken along line B-B in Fig.
The figure is a sectional view taken along the line CC in FIG.
図に示すように従来の積層式熱交換器は、溝加工した熱
交換板1を1枚ごとに900ずつ回転させて積み重ね、
溝から流体2,3が漏れないように熱交換板1および端
板4,5を密着させ、流体2の入口管6,7と出口管8
,9をヘッダー10゜11、 12.13fIJ上に設
け、入口管6,7とヘッダー10.11とが直接つなが
る構造を有していた。As shown in the figure, the conventional stacked heat exchanger consists of grooved heat exchange plates 1 that are stacked by rotating each plate 900 times.
The heat exchange plate 1 and the end plates 4 and 5 are brought into close contact with each other so that the fluids 2 and 3 do not leak from the grooves, and the inlet pipes 6 and 7 of the fluid 2 and the outlet pipe 8 are
, 9 were installed on the headers 10.degree.
入口管6より流入した流体2はヘッダー10に入シ、溝
14a、14bに分岐し流出する。そしてもう一方のヘ
ッダー12で集められ出口管8より流出する。7は他流
体3の入口管、11.13は他流体3のヘッダー、9は
他流体3の出口管であシ、熱交換板1を90°ずつ回転
させ積み菫ね−枚ごとに異なる流体2,3が流れる構造
になる。The fluid 2 flowing in from the inlet pipe 6 enters the header 10, branches into grooves 14a and 14b, and flows out. Then, it is collected by the other header 12 and flows out from the outlet pipe 8. 7 is the inlet pipe for the other fluid 3, 11.13 is the header for the other fluid 3, and 9 is the outlet pipe for the other fluid 3. Rotate the heat exchange plates 1 by 90 degrees and stack them - each plate has a different fluid. 2 and 3 form a flowing structure.
したがって溝14a、14bが熱交換部となり、上下双
方の異なる流体2,3の間で熱交換を行う。Therefore, the grooves 14a and 14b serve as heat exchange parts, and heat exchange is performed between the different fluids 2 and 3 on both the upper and lower sides.
発明が解決しようとする課題
しかしながら上記のような構成では、入口管6とヘッダ
ー10とが直接つながっているので、入口管6から流入
した流体2が入口管6線上の近傍にある溝14aに多く
流れ、入口管6線上の遠方の溝14bに流体2が流れに
くくなり溝14bが伝熱面として有効に活用されず熱交
換性能が低下するという課題があった。Problems to be Solved by the Invention However, in the above configuration, since the inlet pipe 6 and the header 10 are directly connected, a large amount of the fluid 2 flowing from the inlet pipe 6 flows into the groove 14a located near the line of the inlet pipe 6. There was a problem in that the fluid 2 was difficult to flow into the grooves 14b located far away on the inlet pipe 6 line, and the grooves 14b were not effectively utilized as heat transfer surfaces, resulting in a decrease in heat exchange performance.
そこで、本発明は上記課題に鑑み、谷溝に均一に流体を
分岐させることで熱交換性能を向上させるものである。In view of the above problems, the present invention improves heat exchange performance by uniformly branching fluid into valley grooves.
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積層式熱交換器は、
流体の入口管と出口管を有する端板と、内部を流体が流
動する複数の溝と前記溝に連通ずるヘッダーと前記ヘッ
ダーと分離されている他のヘッダーとを具備する熱交換
板を複数枚積層し、前記入口管と前記ヘッダーとの間に
、前記入口管内径より長い辺と前記入口管内径より短い
辺とから成る矩径状の開口部をもつ空間部を設けたもの
である。Means for Solving the Problems In order to solve the above problems, the laminated heat exchanger of the present invention has the following features:
A plurality of heat exchange plates each having an end plate having an inlet pipe and an outlet pipe for fluid, a plurality of grooves through which a fluid flows, a header communicating with the grooves, and another header separated from the header. A space is provided between the inlet pipe and the header and has a rectangular opening having a side longer than the inner diameter of the inlet pipe and a side shorter than the inner diameter of the inlet pipe.
作 用
本発明は、上記した構成によって、流体の入口管とヘッ
ダーとの間の空間部で流体が拡散され、ヘッダーに均一
に流体を分布させることができ、谷溝へ均一に流体を流
すことができる。Effects According to the present invention, with the above-described configuration, the fluid is diffused in the space between the fluid inlet pipe and the header, and the fluid can be uniformly distributed in the header, thereby allowing the fluid to flow uniformly into the valley groove. I can do it.
実施例
以下本発明の一実施例の積層式熱交換器について図面と
ともに説明する。EXAMPLE Hereinafter, a stacked heat exchanger according to an example of the present invention will be explained with reference to the drawings.
第2図は本発明の積層式熱交換器の斜視図、第1図は第
2図のA−A断面図、第3図は本発明の積層式熱交換器
を構成する空間部を有するプレートの斜視図、第4図は
入口管、出口管と空間部との位置関係を示す正面図であ
る。FIG. 2 is a perspective view of the laminated heat exchanger of the present invention, FIG. 1 is a sectional view taken along line A-A in FIG. 2, and FIG. 3 is a plate having a space constituting the laminated heat exchanger of the present invention. FIG. 4 is a front view showing the positional relationship between the inlet pipe, the outlet pipe, and the space.
図に示すように本発明の積層式熱交換器は、溝加工した
熱交換板1を1枚ごとに900ずつ回転させて積み重ね
、その上に入口管6,7に連通する開口部が入口管内径
りより長い辺りと短い辺Sとよ構成る空間部15.16
を有するプレート19と端板4,5を重ね、流体2,3
が漏れないように密着させ、流体2,3の入口管6,7
と出口管8.9を取シ付けた構造である。As shown in the figure, in the stacked heat exchanger of the present invention, grooved heat exchange plates 1 are rotated 900 degrees each and stacked, and openings communicating with inlet pipes 6 and 7 are formed on the inlet pipes. A space portion 15.16 consisting of an area longer than the inner diameter and a shorter side S
The plate 19 having a
The inlet pipes 6 and 7 for the fluids 2 and 3 are tightly connected to prevent leakage.
It has a structure in which an outlet pipe 8.9 is attached.
入口管6より流入した流体2は空間部15を通電ヘツダ
−10に流入し、溝14a、14bに分岐し流出する。The fluid 2 flowing in from the inlet pipe 6 flows into the energizing header 10 through the space 15, branches into grooves 14a and 14b, and flows out.
そしてもう一方のヘッダー12で集められ空間部17を
通電出ロ管8より流出する。Then, it is collected by the other header 12 and flows out from the space 17 through the energized outlet pipe 8.
7は他流体3の入口管、16.18は他流体3側の空間
、11.13は他流体3のヘッダー、9は他流体の出口
管であシ、熱交換板1を90°ずつ回転させ積み重ね一
枚ごとに異なる流体2,3が流れる構造になる。したが
って溝14a、14bが熱交換部となシ、上下双方の異
なる流体2,3の間で熱交換を行う。7 is the inlet pipe for the other fluid 3, 16.18 is the space on the side of the other fluid 3, 11.13 is the header for the other fluid 3, 9 is the outlet pipe for the other fluid, and the heat exchange plate 1 is rotated by 90 degrees. The structure is such that different fluids 2 and 3 flow through each stacked sheet. Therefore, the grooves 14a and 14b serve as heat exchange parts, and heat exchange is performed between the different fluids 2 and 3 on both the upper and lower sides.
本実施例では、入口管6より流入した流体2は、空間部
16に流入したときに絞られ空間部15内部で分散され
、ヘッダー10に均一に分散する。In this embodiment, the fluid 2 flowing in from the inlet pipe 6 is throttled when flowing into the space 16 and dispersed inside the space 15, and is uniformly dispersed in the header 10.
ヘッダー10に均一に分散した流体2は、溝14a。The fluid 2 uniformly dispersed in the header 10 flows through the grooves 14a.
14bに均一に分岐する事ができるので、熱交換性能の
向上が図れる。14b, the heat exchange performance can be improved.
発明の効果
以上のように本発明は、流体の入口管と出口管を有する
端板と、内部を流体が流動する複数の溝と前記溝に連通
ずるヘッダーと前記ヘッダーと分離されている他のヘッ
ダーとを具備する熱交換板を複数枚積層し、前記入口管
と前記ヘッダーとの間に、前記入口管内径より長い辺と
前記入口管内径より短い辺とから成る矩径状の開口部を
もつ空間部を設けたことにより、流体を谷溝へと均一に
分岐させることが可能となり、熱交換性能を著しく向上
させることができる。Effects of the Invention As described above, the present invention provides an end plate having an inlet pipe and an outlet pipe for fluid, a plurality of grooves through which a fluid flows, a header communicating with the grooves, and another device separated from the header. A plurality of heat exchange plates each having a header are laminated, and a rectangular opening having a side longer than the inner diameter of the inlet pipe and a side shorter than the inner diameter of the inlet pipe is formed between the inlet pipe and the header. The provision of the space allows the fluid to branch uniformly into the valley grooves, thereby significantly improving heat exchange performance.
第1図は本発明の実施例における積層式熱交換器の要部
断面図、第2図は同積層式熱交換器の斜視図、第3図は
同積層式熱交換器を構成するプレートの斜視図、第4図
は同積層式熱交換器の正面図、M6図は従来の積層式熱
交換器の斜視図、第6図は同積層式熱交換器を構成する
熱交換板の斜夜回、第7図は第4図のB−B断面図、第
8図は第4図のC−C断面図である。
1・・・・・・熱交換板、4,5・・・・・・端板、6
,7・・・・・・入口管、8,9・・・・・・出口管、
10,11,12゜13・・・・・・ヘッダー 1ea
、 14b・・・・・・溝、15゜16.17.18
・・・・・・空間部。Fig. 1 is a sectional view of the main parts of a laminated heat exchanger according to an embodiment of the present invention, Fig. 2 is a perspective view of the laminated heat exchanger, and Fig. 3 is a view of the plates constituting the laminated heat exchanger. A perspective view, FIG. 4 is a front view of the same laminated heat exchanger, M6 is a perspective view of a conventional laminated heat exchanger, and FIG. 6 is a slanted view of the heat exchange plate making up the same laminated heat exchanger. 7 is a sectional view taken along line BB in FIG. 4, and FIG. 8 is a sectional view taken along line CC in FIG. 4. 1... Heat exchange plate, 4, 5... End plate, 6
, 7... Inlet pipe, 8, 9... Outlet pipe,
10、11、12゜13・・・・・・Header 1ea
, 14b...Groove, 15°16.17.18
・・・・・・Space part.
Claims (1)
動する複数の溝と前記溝に連通するヘッダーと前記ヘッ
ダーと分離されている他のヘッダーとを具備する熱交換
板を複数枚積層し、前記入口管と前記ヘッダーとの間に
、前記入口管内径より長い辺と前記入口管内径より短い
辺とから成る矩径状の開口部をもつ空間部を設けたこと
を特徴とする積層式熱交換器。A plurality of heat exchange plates each having an end plate having an inlet pipe and an outlet pipe for fluid, a plurality of grooves through which a fluid flows, a header communicating with the grooves, and another header separated from the header. A space is provided between the inlet pipe and the header and has a rectangular opening having a side longer than the inner diameter of the inlet pipe and a side shorter than the inner diameter of the inlet pipe. Laminated heat exchanger.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4762290A JP2695269B2 (en) | 1990-02-28 | 1990-02-28 | Stacked heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4762290A JP2695269B2 (en) | 1990-02-28 | 1990-02-28 | Stacked heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03251690A true JPH03251690A (en) | 1991-11-11 |
JP2695269B2 JP2695269B2 (en) | 1997-12-24 |
Family
ID=12780313
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4762290A Expired - Fee Related JP2695269B2 (en) | 1990-02-28 | 1990-02-28 | Stacked heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2695269B2 (en) |
-
1990
- 1990-02-28 JP JP4762290A patent/JP2695269B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2695269B2 (en) | 1997-12-24 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |