JPH04340070A - Condenser - Google Patents

Condenser

Info

Publication number
JPH04340070A
JPH04340070A JP11036191A JP11036191A JPH04340070A JP H04340070 A JPH04340070 A JP H04340070A JP 11036191 A JP11036191 A JP 11036191A JP 11036191 A JP11036191 A JP 11036191A JP H04340070 A JPH04340070 A JP H04340070A
Authority
JP
Japan
Prior art keywords
path
refrigerant
header
condenser
sectional area
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
Application number
JP11036191A
Other languages
Japanese (ja)
Other versions
JP3218053B2 (en
Inventor
Hironaka Sasaki
広仲 佐々木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Altemira Co Ltd
Original Assignee
Showa Aluminum Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Showa Aluminum Corp filed Critical Showa Aluminum Corp
Priority to JP11036191A priority Critical patent/JP3218053B2/en
Publication of JPH04340070A publication Critical patent/JPH04340070A/en
Application granted granted Critical
Publication of JP3218053B2 publication Critical patent/JP3218053B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/0535Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05383Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D2001/0253Particular components
    • F28D2001/026Cores
    • F28D2001/0266Particular core assemblies, e.g. having different orientations or having different geometric features
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D2001/0253Particular components
    • F28D2001/026Cores
    • F28D2001/028Cores with empty spaces or with additional elements integrated into the cores

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Air-Conditioning For Vehicles (AREA)

Abstract

PURPOSE:To improve heat exchange efficiency by partitioning a header so as to pass refrigerant in a zigzag manner in such a way that the sectional area of a refrigerant passage of at least one path of paths other than a first zigzag path is larger than that of the first path. CONSTITUTION:In a multiflow condenser with a recessed part, gas refrigerant entering from an inlet pipe 11 passes through a first path P1 comprising seven shorter tubes 3, then turns to and passes through a second path P2 comprising nine longer tubes 1, further turns to and passes through a third path, namely, a final path P3 comprising five longer tubes 1 and flows in liquefied state out of an outlet pipe 12. The sectional area of the passage of the final path P3 through which the liquefied refrigerant passes is so set as to be smaller than that of the first path P1, so that the inactive core parts of a heat exchanger can be decreased and the heat exchanger with excellent efficiency can be realized.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】この発明は、カークーラー用凝縮
器等に用いられるアルミニウム等の金属製熱交換器に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a metal heat exchanger made of aluminum or the like used in a car cooler condenser or the like.

【0002】0002

【従来の技術】近時、例えばカークーラー用凝縮器とし
て、高熱交換性能、低圧力損失を実現しうる、いわゆる
マルチフロータイプ、あるいはパラレルフロータイプと
称される熱交換器が好んで使用される傾向にある。
[Prior Art] Recently, so-called multi-flow type or parallel flow type heat exchangers, which can achieve high heat exchange performance and low pressure loss, have been preferably used as condensers for car coolers, for example. There is a tendency.

【0003】この熱交換器は、第3図に示されるように
、並列状態にされた多数本の偏平チューブ(51)と、
これらチューブ(51)の両端に連通状態に接続された
一対の中空ヘッダー(52)(52)と、ヘッダー(5
2)に設けられた冷媒入口管(53)と、同出口管(5
4)とを具備するもので、かつ、ヘッダー(52)内が
仕切(55)によって仕切られることによって、熱交換
器内を流通する冷媒の通路断面積が入口側から出口側に
向かって減少されていく態様において、冷媒が蛇行しな
がら熱交換器内を流通するものとなされている。なお、
このように冷媒の通路断面積を減少させていく構成とし
ているのは、凝縮器では、冷媒が、体積の大きいガスの
かたちで流入し、凝縮されて体積の小さい液のかたちで
流出するため、凝縮済みの液冷媒が流通される通路の断
面積を小さくすることによって熱交換が不活発な無駄な
部分を少なくして熱交換効率を高めるためである。なお
、(56)はコルゲートフィンである。
As shown in FIG. 3, this heat exchanger includes a large number of flat tubes (51) arranged in parallel;
A pair of hollow headers (52) (52) are connected to both ends of these tubes (51) in a communicating state, and a header (5
2) and the refrigerant inlet pipe (53) provided in the refrigerant outlet pipe (53).
4), and by partitioning the inside of the header (52) with the partition (55), the passage cross-sectional area of the refrigerant flowing inside the heat exchanger is reduced from the inlet side to the outlet side. In several embodiments, the refrigerant flows through the heat exchanger in a meandering manner. In addition,
The reason why the refrigerant passage cross-sectional area is reduced in this way is that in the condenser, the refrigerant enters in the form of a gas with a large volume, and is condensed and flows out in the form of a liquid with a small volume. This is to increase heat exchange efficiency by reducing the cross-sectional area of the passage through which the condensed liquid refrigerant flows, thereby reducing wasteful areas where heat exchange is inactive. Note that (56) is a corrugated fin.

【0004】ところで、自動車においては、昨今の居住
空間の拡大に伴うエンジンルームの縮小化傾向により、
エンジンルーム内におけるエアコン用凝縮器の配置に関
しても、他の装置等との関係で無駄なスペースをなくし
、効率良くこれを配備することが要請されている。
By the way, in automobiles, due to the recent tendency to reduce the size of the engine room due to the expansion of living space,
Regarding the arrangement of the air conditioner condenser in the engine room, there is a need to eliminate wasted space in relation to other devices and to arrange it efficiently.

【0005】そこで、エンジンルーム内に凝縮器の配置
を妨げる障害物等が有る場合、無駄なスペースの発生を
阻止しつつ障害物を避けて凝縮器を配置するため、上記
マルチフロータイプの凝縮器を次のように構成すること
が提案されている。
[0005] Therefore, when there is an obstacle that obstructs the placement of the condenser in the engine room, the above-mentioned multi-flow type condenser is used in order to avoid wasting space and avoid the obstacle. It is proposed to configure the following.

【0006】即ち、例えば、第4図に示されるように、
並列状態に配置された複数本の偏平チューブ(61)(
62)からなる長さの異なる2つのチューブ群(63)
(64)が並列状態に配置され、両チューブ群(63)
(64)の一端を揃えて両者間にかけわたし状態に長尺
な中空ヘッダー(65)が連通接続されると共に、両チ
ューブ群(63)(64)の他端のそれぞれに個別に短
尺な中空ヘッダー(66)(67)が連通接続され、短
尺チューブ(61)からなるチューブ群(63)の端部
に接続された短尺ヘッダー(66)を、長尺チューブ(
62)からなるチューブ群(64)の端部に接続された
短尺ヘッダー(67)よりもコア内方に退入させて、障
害物回避用の凹部(68)が設けられたものとなされて
いる。
That is, for example, as shown in FIG.
A plurality of flat tubes (61) arranged in parallel (
Two groups of tubes (63) with different lengths consisting of (62)
(64) are arranged in parallel, both tube groups (63)
A long hollow header (65) is connected in communication with one end of the tube group (64) extending between them, and a short hollow header is attached to each of the other ends of both tube groups (63) and (64). (66) and (67) are connected in communication, and a short header (66) connected to the end of a tube group (63) consisting of short tubes (61) is connected to a long tube (
A recess (68) for avoiding obstacles is provided inwardly of the short header (67) connected to the end of the tube group (64) consisting of the tube group (62). .

【0007】[0007]

【発明が解決しようとする課題】しかしながら、マルチ
フロータイプの熱交換器を、上記のように、凹部(68
)付きに構成した場合、冷媒の流れを考慮した最適な仕
切り(69)の設置位置と、熱交換器の設置スペースを
考慮した最適な凹部(68)の大きさ、位置との関係に
ギャップを生じて、往々にして、第4図に示されるよう
に、ヘッダー(65)(66)(67)内を多数箇所に
おいて仕切(69)にて仕切ったものとしなければ、冷
媒の液・ガス状態を考慮した通路断面積の漸次的減少を
実現することが困難となり、そのため、逆に冷媒側の圧
力損失が大きくなりすぎてかえって熱交換効率を悪くし
てしまうという欠点が派生した。
[Problems to be Solved by the Invention] However, as described above, the multi-flow type heat exchanger is
), there is a gap in the relationship between the optimal installation position of the partition (69) considering the flow of refrigerant and the optimal size and position of the recess (68) considering the installation space of the heat exchanger. As shown in FIG. 4, unless the headers (65), (66, and 67) are partitioned at multiple locations with partitions (69), the liquid/gas state of the refrigerant will often change. It became difficult to realize a gradual reduction in the cross-sectional area of the passage in consideration of the above, and as a result, the pressure loss on the refrigerant side became too large, which resulted in a disadvantage that the heat exchange efficiency worsened.

【0008】この発明は、かかる問題点を解決し、全体
として調和のとれた熱交換効率の向上を図ることができ
る凹部付きマルチフロー凝縮器を提供することを目的と
する。
[0008] An object of the present invention is to provide a multi-flow condenser with recesses that can solve the above problems and improve the heat exchange efficiency in a well-balanced manner as a whole.

【0009】[0009]

【課題を解決するための手段】上記目的において、この
発明は、並列状態に配置された複数本のチューブからな
る長さの異なる複数のチューブ群が並列状態に配置され
、隣接するチューブ群の一端にかけわたし状態に中空ヘ
ッダーが連通接続されると共に、当該両チューブ群の他
端のそれぞれに個別に中空ヘッダーが連通接続されて、
コアに、ヘッダーの退入した凹部が形成された凝縮器に
おいて、冷媒が蛇行しながら流通するように、上記ヘッ
ダー内が、蛇行の第1パス以外の他のパスの少なくとも
1つのパスの冷媒通路断面積を第1パスの冷媒通路断面
積よりも大にする態様において、仕切られてなることを
特徴とする凝縮器を要旨とする。
[Means for Solving the Problems] To achieve the above object, the present invention provides a method in which a plurality of tube groups having different lengths each including a plurality of tubes arranged in a parallel state are arranged in a parallel state, and one end of the adjacent tube group is arranged in a parallel state. A hollow header is connected in communication in a crossed state, and a hollow header is individually connected in communication to each of the other ends of both the tube groups,
In a condenser in which a recessed portion of the header is formed in the core, the refrigerant passage in the header is at least one path other than the first meandering path so that the refrigerant flows in a meandering manner. The gist of the present invention is a condenser that is partitioned in such a manner that its cross-sectional area is larger than the cross-sectional area of a first pass refrigerant passage.

【0010】0010

【作用】上記構成は、冷媒の液・ガス状態を考慮した冷
媒通路構成、即ち、冷媒通路断面積を入口側から出口側
に向けて所定の態様に減少させていく構成を採用するも
のではない。しかし、蛇行の第1パス以外の他のパスの
少なくとも1つのパスの冷媒通路断面積が第1パスの冷
媒通路断面積よりも大にした冷媒通路構成としているこ
とにより、凹部付きマルチフロー凝縮器において、多く
の場合に、各パスの通路断面積を大きく確保できて冷媒
側圧力損失を小さくでき、これにより、全体としての熱
交換効率は、逆に向上される。
[Operation] The above configuration does not adopt a refrigerant passage configuration that takes into account the liquid/gas state of the refrigerant, that is, a configuration in which the cross-sectional area of the refrigerant passage is reduced in a predetermined manner from the inlet side to the outlet side. . However, by adopting a refrigerant passage configuration in which the refrigerant passage cross-sectional area of at least one path other than the meandering first path is larger than the refrigerant passage cross-sectional area of the first path, the recessed multiflow condenser In many cases, it is possible to ensure a large passage cross-sectional area for each path, thereby reducing the pressure loss on the refrigerant side, and thereby improving the overall heat exchange efficiency.

【0011】[0011]

【実施例】次に、この発明の凝縮器をカークーラー用ア
ルミニウム製凝縮器に適用した実施例を図面に基いて説
明する。なお、本発明の凝縮器は、ルームエアコン用の
凝縮器等の各種の凝縮器にも適用され得るものであるこ
とはいうまでもない。
[Embodiment] Next, an embodiment in which the condenser of the present invention is applied to an aluminum condenser for a car cooler will be described with reference to the drawings. It goes without saying that the condenser of the present invention can also be applied to various types of condensers such as condensers for room air conditioners.

【0012】第1図に示される凝縮器は、14本の長尺
な偏平チューブ(1)を並列状態に配置した長尺チュー
ブ群(2)と、7本の短尺チューブ(3)を並列状態に
配置して形成された短尺チューブ群(4)とを有してい
る。これらのチューブ群(2)(4)は、長尺チューブ
群(2)を下にし、短尺チューブ群(4)を上にして、
かつ両チューブ群(2)(4)の一端を揃えた状態に、
互いに並列状態となるように配置されている。
The condenser shown in FIG. 1 consists of a long tube group (2) in which 14 long flat tubes (1) are arranged in parallel, and a long tube group (2) in which 7 short tubes (3) are arranged in parallel. It has a short tube group (4) arranged and formed. These tube groups (2) and (4) are arranged with the long tube group (2) at the bottom and the short tube group (4) at the top.
And with one end of both tube groups (2) and (4) aligned,
They are arranged in parallel to each other.

【0013】そして、両チューブ群(2)(4)の揃い
側の端部にかけわたし状態に長尺な中空ヘッダー(5)
が連通状態に接続され、かつ、短尺チューブ群(4)及
び長尺チューブ群(2)の他端部のそれぞれに、個別に
、短尺な中空ヘッダー(6)(7)が連通状態に接続さ
れている。これにより、コア(8)に、上部側短尺ヘッ
ダー(6)が退入した凹部(9)が形成されている。
[0013] A long hollow header (5) is placed across the ends of both tube groups (2) and (4) on the same side.
are connected in a communicating state, and short hollow headers (6) and (7) are individually connected in a communicating state to the other ends of the short tube group (4) and the long tube group (2), respectively. ing. As a result, a recess (9) into which the upper short header (6) is retracted is formed in the core (8).

【0014】そして、下から5本目の長尺チューブ(1
)と6本目の長尺チューブ(1)との間の位置において
、長尺ヘッダー(5)内が仕切(10)により上下の室
に分割されている。そして、上側短尺ヘッダー(6)に
冷媒の入口管(11)が接続されると共に、長尺ヘッダ
ー(5)の下端部側面に冷媒の出口管(12)が接続さ
れている。なお、(13)はコルゲートフィン、(14
)は、フィン保護用のサイドプレートである。
[0014] Then, the fifth long tube from the bottom (1
) and the sixth long tube (1), the inside of the long header (5) is divided into upper and lower chambers by a partition (10). A refrigerant inlet pipe (11) is connected to the upper short header (6), and a refrigerant outlet pipe (12) is connected to the side surface of the lower end of the long header (5). In addition, (13) is a corrugated fin, (14)
) is a side plate for fin protection.

【0015】なお、各熱交換器構成部材はアルミニウム
製で、熱交換器の製作は、例えば、各構成部材を、相互
に仮組状態に組み合わせ、その組立状態において、全体
を一括ろう付けにより相互に接合一体化することなどに
より行われる。その場合、ヘッダー(5)(6)(7)
とチューブ(1)(3)との仮組は、図示しないが、例
えば、ヘッダー(5)(6)(7)の周側面に形成した
周方向スリット状のチューブ挿入孔を通じて同ヘッダー
内に内方突出状態に偏平チューブ(1)(2)の端部を
挿入配置することなどにより行う。
Each of the heat exchanger components is made of aluminum, and the heat exchanger is manufactured by, for example, assembling each component into a temporary assembly state, and then brazing the entire assembly together in the assembled state. This is done by joining and integrating the parts. In that case, header (5) (6) (7)
Although not shown, the temporary assembly of the tubes (1) and (3) is carried out, for example, by inserting the tubes into the headers (5), (6), and (7) through tube insertion holes in the form of circumferential slits formed on the circumferential sides of the headers (5), (6), and (7). This is done by inserting and arranging the ends of the flat tubes (1) and (2) so that they protrude in the opposite direction.

【0016】上記構成の凹部付きマルチフロー凝縮器で
は、入口管(11)から流入したガス冷媒は、7本の短
尺チューブ(3)からなる第1パス(P1)を通過した
のち、向きを変えて9本の長尺チューブ(1)からなる
第2パス(P2 )を通過し、また向きを変えて5本の
長尺チューブ(1)からなる第3パス、即ち最終パス(
P3 )を通過し、そして、出口管(12)から液状と
なって流出する。このように、蛇行の第1パス(P1 
)以外の他のパスのいずれか少なくとも1つのパスの冷
媒通路断面積を第1パス(P1)の通路断面積よりも大
きく設定した構成とすることにより、凹部付きマルチフ
ロー凝縮器において、その冷媒蛇行回数を減少せしめて
各パスの通路断面積の拡大を図ることができ、圧力損失
も考慮した全体としての熱交換効率を向上することがで
きる。
[0016] In the multi-flow condenser with recesses configured as described above, the gas refrigerant flowing in from the inlet pipe (11) changes direction after passing through the first path (P1) consisting of seven short tubes (3). It passes through the second pass (P2) consisting of nine long tubes (1), then changes direction and passes through the third pass (P2) consisting of five long tubes (1), that is, the final pass (
P3) and then flows out in liquid form from the outlet pipe (12). In this way, the first path of meandering (P1
), the refrigerant passage cross-sectional area of at least one of the other paths other than ) is set larger than the passage cross-sectional area of the first pass (P1). It is possible to increase the passage cross-sectional area of each path by reducing the number of meanderings, and it is possible to improve the overall heat exchange efficiency in consideration of pressure loss.

【0017】また、図示実施例のように、液状冷媒の通
過通過する最終パス(P3 )の通路断面積を第1パス
(P1 )のそれよりも小さく設定することにより、熱
交換の不活発なコア部分の減少を図ることができ、いよ
いよ効率よい熱交換が実現される。
Furthermore, as in the illustrated embodiment, by setting the passage cross-sectional area of the final pass (P3) through which the liquid refrigerant passes smaller than that of the first pass (P1), heat exchange is inactive. The core portion can be reduced, and more efficient heat exchange can be achieved.

【0018】第2図に示される他の実施例では、9本の
短尺チューブ(3)からなるチューブ群(4)と、25
本の長尺チューブ(1)からなる長尺チューブ群(2)
とを用いたもので、下から14本目の長尺チューブ(1
)と15本目の長尺チューブ(1)との間において長尺
ヘッダー(5)内が仕切(10)によって上下の室に分
割され、かつ、下から4本目の長尺チューブ(1)と5
本目の長尺チューブ(1)との間において下側短尺ヘッ
ダー(7)内が仕切(10)によって上下の室に分割さ
れている。この場合、入口管(11)から流入したガス
冷媒は、9本の短尺チューブ(3)からなる第1パス(
P1 )を通過したのち、向きを変えて11本の長尺チ
ューブ(1)からなる第2パス(P2 )を通過し、ま
た向きを変えて10本の長尺チューブ(1)からなる第
3パス(P3 )を通過し、更に向きを変えて4本の長
尺チューブ(1)からなる第4パス、即ち最終パス(P
4 )を通過し、そして、出口管(12)から液状とな
って流出する。
In another embodiment shown in FIG. 2, a tube group (4) consisting of 9 short tubes (3) and 25
Long tube group (2) consisting of book long tubes (1)
The 14th long tube from the bottom (1
) and the 15th long tube (1), the inside of the long header (5) is divided into upper and lower chambers by a partition (10), and between the 4th long tube (1) from the bottom and the 15th long tube (1)
Between the main long tube (1), the inside of the lower short header (7) is divided into upper and lower chambers by a partition (10). In this case, the gas refrigerant flowing from the inlet pipe (11) passes through the first path (3) consisting of nine short tubes (3).
After passing through P1), it changes direction and passes through the second pass (P2), which consists of 11 long tubes (1), and then changes direction and passes through the third pass, which consists of 10 long tubes (1). pass (P3), change direction and pass the fourth pass consisting of four long tubes (1), that is, the final pass (P
4) and flows out from the outlet pipe (12) as a liquid.

【0019】[0019]

【発明の効果】上述の次第で、この発明の凝縮器は、並
列状態に配置された複数本のチューブからなる長さの異
なる複数のチューブ群が並列状態に配置され、隣接する
チューブ群の一端にかけわたし状態に中空ヘッダーが連
通接続されると共に、当該両チューブ群の他端のそれぞ
れに個別に中空ヘッダーが連通接続されて、コアに、ヘ
ッダーの退入した凹部が形成された凝縮器において、冷
媒が蛇行しながら流通するように、上記ヘッダー内が、
蛇行の第1パス以外の他のパスの少なくとも1つのパス
の冷媒通路断面積を第1パスの冷媒通路断面積よりも大
にする態様において、仕切られたものである。従って、
各パスの通路断面積を大きく確保できて冷媒側圧力損失
を小さくでき、これにより、このような凹部付きマルチ
フロー凝縮器において、全体としての熱交換効率の向上
を図ることができる。
Effects of the Invention As described above, the condenser of the present invention includes a plurality of tube groups having different lengths, each consisting of a plurality of tubes arranged in parallel, and one end of the adjacent tube group. A condenser in which a hollow header is connected in communication in a crossed state, and a hollow header is individually connected in communication to each of the other ends of the two tube groups, and a recess into which the header retracts is formed in the core, The inside of the above header is designed so that the refrigerant flows in a meandering manner.
The refrigerant passage cross-sectional area of at least one path other than the meandering first path is made larger than the refrigerant passage cross-sectional area of the first path. Therefore,
It is possible to ensure a large passage cross-sectional area for each path, thereby reducing the pressure loss on the refrigerant side, thereby making it possible to improve the overall heat exchange efficiency in such a multi-flow condenser with recesses.

【図面の簡単な説明】[Brief explanation of drawings]

【図1】本発明の一実施例にかかる凝縮器を示すもので
、図(イ)は全体正面図、図(ロ)は同平面図である。
FIG. 1 shows a condenser according to an embodiment of the present invention, in which figure (a) is an overall front view and figure (b) is a plan view of the same.

【図2】本発明の他の実施例にかかる凝縮器を示すもの
で、図(イ)は全体正面図、図(ロ)は同平面図である
FIG. 2 shows a condenser according to another embodiment of the present invention, in which FIG. 2A is an overall front view and FIG. 2B is a plan view of the same.

【図3】従来の凝縮器を示すもので、図(イ)は全体正
面図、図(ロ)は全体平面図である。
FIG. 3 shows a conventional condenser, in which figure (a) is an overall front view and figure (b) is an overall plan view.

【図4】従来の他の凝縮器を示すもので、図(イ)は全
体正面図、図(ロ)は全体平面図である。
FIG. 4 shows another conventional condenser, in which figure (a) is an overall front view and figure (b) is an overall plan view.

【符号の説明】[Explanation of symbols]

1…長尺チューブ 2…長尺チューブ群 3…短尺チューブ 4…短尺チューブ群 5…長尺ヘッダー 6、7…短尺ヘッダー 8…コア 9…凹部 10…仕切り P1 …第1パス 1...Long tube 2...Long tube group 3...Short tube 4...Short tube group 5...Long header 6, 7…Short header 8...Core 9...Concavity 10...Partition P1...1st pass

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  並列状態に配置された複数本のチュー
ブからなる長さの異なる複数のチューブ群が並列状態に
配置され、隣接するチューブ群の一端にかけわたし状態
に中空ヘッダーが連通接続されると共に、当該両チュー
ブ群の他端のそれぞれに個別に中空ヘッダーが連通接続
されて、コアに、ヘッダーの退入した凹部が形成された
凝縮器において、冷媒が蛇行しながら流通するように、
上記ヘッダー内が、蛇行の第1パス以外の他のパスの少
なくとも1つのパスの冷媒通路断面積を第1パスの冷媒
通路断面積よりも大にする態様において、仕切られてな
ることを特徴とする凝縮器。
[Claim 1] A plurality of tube groups having different lengths each consisting of a plurality of tubes arranged in parallel are arranged in parallel, and a hollow header is communicatively connected to one end of the adjacent tube group in a crossed state. , a hollow header is individually connected to the other ends of the two tube groups, so that the refrigerant flows in a meandering manner in the condenser in which a recess into which the header is recessed is formed in the core.
The inside of the header is partitioned in such a manner that the refrigerant passage cross-sectional area of at least one path other than the meandering first path is larger than the refrigerant passage cross-sectional area of the first path. condenser.
JP11036191A 1991-05-15 1991-05-15 Condenser Expired - Fee Related JP3218053B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11036191A JP3218053B2 (en) 1991-05-15 1991-05-15 Condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11036191A JP3218053B2 (en) 1991-05-15 1991-05-15 Condenser

Publications (2)

Publication Number Publication Date
JPH04340070A true JPH04340070A (en) 1992-11-26
JP3218053B2 JP3218053B2 (en) 2001-10-15

Family

ID=14533838

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11036191A Expired - Fee Related JP3218053B2 (en) 1991-05-15 1991-05-15 Condenser

Country Status (1)

Country Link
JP (1) JP3218053B2 (en)

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JP2014085047A (en) * 2012-10-23 2014-05-12 Sharp Corp Parallel flow type heat exchanger
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Cited By (10)

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Publication number Priority date Publication date Assignee Title
JP2014085047A (en) * 2012-10-23 2014-05-12 Sharp Corp Parallel flow type heat exchanger
WO2017188146A1 (en) * 2016-04-27 2017-11-02 東芝ライフスタイル株式会社 Refrigerator
WO2017188147A1 (en) * 2016-04-27 2017-11-02 東芝ライフスタイル株式会社 Refrigerator
JP2017201231A (en) * 2016-04-27 2017-11-09 東芝ライフスタイル株式会社 refrigerator
JP2017201230A (en) * 2016-04-27 2017-11-09 東芝ライフスタイル株式会社 refrigerator
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