JP3043051B2 - Heat exchange equipment - Google Patents

Heat exchange equipment

Info

Publication number
JP3043051B2
JP3043051B2 JP2318366A JP31836690A JP3043051B2 JP 3043051 B2 JP3043051 B2 JP 3043051B2 JP 2318366 A JP2318366 A JP 2318366A JP 31836690 A JP31836690 A JP 31836690A JP 3043051 B2 JP3043051 B2 JP 3043051B2
Authority
JP
Japan
Prior art keywords
tube
heat exchange
heat exchanger
air flow
shape
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
Application number
JP2318366A
Other languages
Japanese (ja)
Other versions
JPH04187990A (en
Inventor
広仲 佐々木
啓司 山崎
Original Assignee
昭和アルミニウム株式会社
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 昭和アルミニウム株式会社 filed Critical 昭和アルミニウム株式会社
Priority to JP2318366A priority Critical patent/JP3043051B2/en
Publication of JPH04187990A publication Critical patent/JPH04187990A/en
Application granted granted Critical
Publication of JP3043051B2 publication Critical patent/JP3043051B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • F28D1/047Heat-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 bent, e.g. in a serpentine or zig-zag
    • F28D1/0475Heat-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 bent, e.g. in a serpentine or zig-zag the conduits having a single U-bend
    • F28D1/0476Heat-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 bent, e.g. in a serpentine or zig-zag the conduits having a single U-bend the conduits having a non-circular cross-section
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F17/00Removing ice or water from heat-exchange apparatus
    • F28F17/005Means for draining condensates from heat exchangers, e.g. from evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/26Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
    • F28F9/262Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators for radiators

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Filters, Heat-Exchange Apparatuses, And Housings Of Air-Conditioning Units (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、例えばルームクーラー用室内機等として
使用される熱交換装置に関する。
Description: TECHNICAL FIELD The present invention relates to a heat exchange device used as, for example, an indoor unit for a room cooler.

従来の技術及び課題 従来、ルームクーラー用室内機等の熱交換装置とし
て、拡管タイプの蒸発器即ち多数枚の薄肉板状フィンが
所定間隙を隔てて並列状に配置されると共に、これらフ
ィンに複数本のヘアピン状のパイプが貫通状に差し込ま
れ、かつ拡管されてフィンに密着されると共に、上記パ
イプの各端部どおしがU字状管で連通された型式の蒸発
器を備えた熱交換装置が用いられていた。
2. Description of the Related Art Conventionally, as a heat exchanger such as an indoor unit for a room cooler, a tube-type evaporator, that is, a plurality of thin plate-like fins are arranged in parallel with a predetermined gap, and a plurality of fins are arranged on these fins. A heat pin equipped with a type of evaporator, in which a hairpin-shaped pipe is inserted in a penetrating manner and expanded so as to be in close contact with the fins, and each end of the pipe is communicated with a U-shaped pipe. Exchange equipment was used.

ところが、このような拡管式の蒸発器を用いた熱交換
装置では、熱交換効率の向上に限界があった。
However, in the heat exchange device using such an expansion-type evaporator, there is a limit in improving the heat exchange efficiency.

そこで、上記熱蒸発器に代えて、熱交換効率の一層優
れたいわゆるマルチフロー型と称される蒸発器を用いる
ことが考えられる。この型式の熱交換器は、第4図およ
び第5図に示すように、複数本の偏平チューブ(13)が
並列状に配置されるとともに隣接チューブ間にフィン
(14)が配置され、かつ各チューブ(13)の両端に筒状
中空ヘッダー(11)(12)が連通接続されたものであ
る。同図において、(15)は冷媒入口管、(16)は同出
口管、(C′)はファンである。
Therefore, it is conceivable to use a so-called multi-flow type evaporator which is more excellent in heat exchange efficiency, instead of the heat evaporator. In this type of heat exchanger, as shown in FIGS. 4 and 5, a plurality of flat tubes (13) are arranged in parallel and fins (14) are arranged between adjacent tubes. The tubular hollow headers (11) and (12) are connected to both ends of the tube (13). In the figure, (15) is a refrigerant inlet pipe, (16) is an outlet pipe, and (C ') is a fan.

ところで、ルームエアコン用室内機では、設置スペー
スとの関係で全体を可及的コンパクトにまとめる必要が
ある。従って、コンパクト化のため蒸発器(A′)は第
4図及び第5図に示すように、ケーシング(B′)内の
空気流通路に空気流通方向に対して傾斜して配置される
ことが多い。
By the way, in the indoor unit for the room air conditioner, it is necessary to make the whole as compact as possible in relation to the installation space. Therefore, as shown in FIGS. 4 and 5, the evaporator (A ') may be arranged in the air flow passage in the casing (B') at a slant with respect to the air flow direction for the sake of compactness. Many.

しかしながら、蒸発器を傾斜させて設置してもなお、
全体がかさばりコンパクト化の要請に十分対応すること
はできなかった。もとより、蒸発器の長さを短縮するこ
とでコンパクト化は可能になるが、この場合は熱交換性
能が低下するという別の問題を派生するものであった。
However, even if the evaporator is installed at an angle,
The whole was not able to respond to the demand for bulky and compact. Needless to say, shortening the length of the evaporator makes it possible to reduce the size of the evaporator, but in this case, it has another problem that the heat exchange performance is reduced.

この発明は、上述の問題点を解消すべくなされたもの
で、装置全体のコンパクト化を図ることができ、あるい
は装置を同じ大きさに保った場合には熱交換効率を増大
できる熱交換装置の提供を目的とするものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-described problems, and it is possible to reduce the size of the entire apparatus or to increase the heat exchange efficiency when the apparatus is kept the same size. It is intended to be provided.

課題を解決するための手段 上記目的を達成すべく、この発明は、複数本の偏平チ
ューブとフィンとが交互配置となされるとともに、各チ
ューブの両端が1対の中空ヘッダーに連通接続された熱
交換器を備え、該熱交換器がチューブの長さ方向の中間
部で略V状に曲成されるとともに、空気流通方向に対し
曲成部を風上側とする略逆V形あるいは曲成部を風下側
とする略V形をなして空気流通路に配設されてなる熱交
換装置であって、前記屈成部においてチューブおよびフ
ィンが分割されるとともに、このチューブの分割端部が
前記屈成部に設けられた中間ヘッダーに連通接続されて
なることを特徴とするものである。
Means for Solving the Problems In order to achieve the above-mentioned object, the present invention provides a heat exchanger in which a plurality of flat tubes and fins are alternately arranged, and both ends of each tube are connected to a pair of hollow headers. A heat exchanger which is bent in a substantially V-shape at an intermediate portion in the longitudinal direction of the tube, and which has a bent portion on the windward side in the air flow direction. A heat exchanger having a substantially V-shape disposed in the air flow passage with a leeward side, wherein a tube and a fin are divided at the bending portion, and a divided end of the tube is bent at the bending end. It is characterized in that it is connected to an intermediate header provided in the component part.

作 用 熱交換器が空気流通方向に対し曲成部を風上側とする
略逆V形あるいは曲成部を風下側とする略V形をなして
空気流通路に配置されているから、同一長さのチューブ
を用いた場合には少なくとも空気流通方向における熱交
換器の見掛上の長さを短縮でき、ひいては装置全体をコ
ンパクトにできる。一方、装置の大きさが同じであれ
ば、チューブ長さの長い熱交換器を収容できるから、熱
交換効率が増大する。
The heat exchanger is arranged in the air flow passage in a substantially inverted V-shape with the curved portion on the windward side or a V-shaped shape with the curved portion on the leeward side in the air flow direction. When the tube is used, at least the apparent length of the heat exchanger in the air flow direction can be shortened, and the whole apparatus can be made compact. On the other hand, if the size of the device is the same, a heat exchanger having a long tube length can be accommodated, so that the heat exchange efficiency increases.

また、一方のチューブ群から流入した冷媒が一旦中間
ヘッダーで合流され、撹拌されてから他方のチューブ群
に流出することになり、両端にのみヘッダーが存在する
場合に較べて熱交換効率が向上する。
In addition, the refrigerant that has flowed in from one of the tube groups is once merged in the intermediate header, and then flows out to the other tube group after being stirred, so that the heat exchange efficiency is improved as compared with the case where the header exists only at both ends. .

実施例 以下、この発明をルームエアコン用室内機として用い
られる熱交換装置に適用した図示実施例に基づいて説明
する。
Embodiment Hereinafter, a description will be given based on an illustrated embodiment in which the present invention is applied to a heat exchange device used as an indoor unit for a room air conditioner.

第1図および第2図に示す熱交換装置において、
(B)はケーシング、(A)は該ケーシング内に収容さ
れた蒸発器、(C)は蒸発器の下方中央に配置されたフ
ァンである。
In the heat exchange device shown in FIGS. 1 and 2,
(B) is a casing, (A) is an evaporator housed in the casing, and (C) is a fan arranged at the lower center of the evaporator.

前記蒸発器(A)は、両端に一対のヘッダー(1)
(2)が配置されると共に側面視略逆V字状に曲成され
たコア部(7)を有する。このコア部(7)は、所定間
隙を隔てて並列状に配置された複数本の偏平チューブ
(3)とそれらの空気流通間隙に介在配置されたフィン
(4)とで構成されている。前記偏平チューブ(3)は
アルミニウム材による押出型材をもって構成されたもの
であり、耐圧性を向上させる目的で内部に補強壁を有す
るいわゆるハモニカチューブと称される偏平多孔押出型
材が好適に用いらる。もっとも、かかる押出型材に代え
て電縫管等を用いても良い。上記隣接チューブ(3)間
に介在配置されたフィン(4)は、蛇行状に曲成された
いわゆるコルゲートフィンであり、ろう付によりチュー
ブ(3)に接合されている。フィン(4)は、望ましく
はルーバーを切り起こしたものを用いるのが良く、また
熱交換効率向上の目的でチューブ(3)より広幅状に設
定されたものを用いても良い。
The evaporator (A) has a pair of headers (1) at both ends.
(2) is arranged and has a core part (7) bent in a substantially inverted V-shape in side view. The core part (7) is composed of a plurality of flat tubes (3) arranged in parallel with a predetermined gap therebetween and fins (4) interposed in the air flow gap. The flat tube (3) is formed of an extruded member made of an aluminum material. For the purpose of improving pressure resistance, a flat porous extruded member called a so-called harmonica tube having a reinforcing wall therein is preferably used. . However, an electric resistance welded tube or the like may be used in place of such an extruded die. The fin (4) interposed between the adjacent tubes (3) is a so-called corrugated fin bent in a meandering shape, and is joined to the tube (3) by brazing. The fins (4) are desirably cut and raised louvers, and may be wider than the tubes (3) for the purpose of improving heat exchange efficiency.

上記コア部(7)の両端に連通接続された一対のヘッ
ダー(1)(2)は、それぞれ一本の断面円形のアルミ
ニウム製パイプ材をもって形成されたものである。これ
らヘッダー(1)(2)には、チューブ挿入孔(1a)
(2a)が穿設されると共に、該挿入孔(1a)(2a)に上
記各チューブ(3)の端部が挿入され、かつろう付によ
り液密状態に強固に接合連結されている。
The pair of headers (1) and (2) connected to both ends of the core portion (7) are each formed of one aluminum pipe material having a circular cross section. These headers (1) and (2) have tube insertion holes (1a)
(2a) is drilled, and the ends of the tubes (3) are inserted into the insertion holes (1a) and (2a), and are firmly connected in a liquid-tight state by brazing.

なお、上記ろう付に関しては、ヘッダー(1)(2)
を外面にろう材層が被覆形成されたブレージングシート
からなる電縫管により、またフィン(4)をブレージン
グシートによりそれぞれ形成し、各ヘッダー(1)
(2)、チューブ(3)およびフィン(4)を仮組した
状態で真空加熱炉等に搬入し、これらを一括ろう付にて
接合一体化するものとなすのが、生産性を向上する点で
極めて望ましい。
As for the above brazing, headers (1) and (2)
Are formed by an electric resistance welded tube made of a brazing sheet having a brazing material layer formed on the outer surface thereof, and the fins (4) are formed by the brazing sheet.
(2) The productivity is improved by carrying the tubes (3) and the fins (4) in a temporarily assembled state into a vacuum heating furnace or the like and joining them together by brazing. Is highly desirable.

上記チューブ(3)およびフィン(4)で構成された
コア部(7)は、チューブ(3)の長さ方向の中間の曲
成部(70)において側面視略逆V字状に曲成されてい
る。そして、この曲成部(70)においてチューブ(3)
及びフィン(4)が左右に分割されるとともに、曲成部
(70)に設けられた中間ヘッダー(9)にチューブ
(3)の分割端部が連通接続されているものである。さ
らにまた、中間ヘッダー(9)の両側のチューブ群が半
チューブピッチずつずれた交互配置状態でこの中間ヘッ
ダー(9)に連結されている。
The core portion (7) composed of the tube (3) and the fins (4) is bent at a middle bent portion (70) in the longitudinal direction of the tube (3) into a substantially inverted V shape in a side view. ing. Then, in this curved part (70), the tube (3)
And the fins (4) are divided right and left, and the divided end of the tube (3) is connected to an intermediate header (9) provided in the bent portion (70). Furthermore, the tube groups on both sides of the intermediate header (9) are connected to the intermediate header (9) in an alternately arranged state shifted by a half tube pitch.

また、一方のヘッダー(2)の一端外側面には冷媒入
口管(5)が取着されると共に、他方のヘッダー(1)
の他端外側面には冷媒出口管(6)が取着されている。
而して、冷媒入口管(5)から流入した冷媒は第2図に
示すようにチューブ(3)で構成される全冷媒通路を流
通して冷媒出口管(6)から流出し、この間にチューブ
(3)(3)間に形成されたフィン(4)を含む空気流
通間隙を流通する空気と熱交換を行い、蒸発するものと
なされている。
A refrigerant inlet pipe (5) is attached to the outer surface of one header (2) at one end, and the other header (1)
A refrigerant outlet pipe (6) is attached to the outer surface of the other end.
As shown in FIG. 2, the refrigerant flowing from the refrigerant inlet pipe (5) flows through all the refrigerant passages constituted by the tubes (3) and flows out of the refrigerant outlet pipe (6). (3) It exchanges heat with air flowing through the air flow gap including the fins (4) formed between (3) and evaporates.

上記蒸発器は、第1図に示すように、下向きの空気流
通方向Wに対し曲成部(70)が風上側に位置する略逆V
形をなして空気流通路に配置されている。
As shown in FIG. 1, the evaporator has a substantially reverse V in which the bent portion (70) is located on the windward side with respect to the downward air flow direction W.
A shape is arranged in the air flow passage.

第1図に示す熱交換装置では、ファン(C)により吸
入空気は蒸発器(A)のコア部(7)全体を均等に通過
したのちケーシング(B)の外部に吹き出される。この
間に空気は蒸発器のチューブ(3)内を流通する冷媒と
熱交換して冷却される。また、図示のように蒸発器
(A)が空気流通方向に対し略逆V形をなして設置され
ることにより、特に次のような利点がある。即ち、チュ
ーブ(3)の表面には流通空気の凝縮から生じる結露水
が付着するが、この結露水は流通空気の付勢力によって
チューブを伝って両側ヘッダー方向に移動する。従って
コア部(7)の中央部分に生じた結露水がそのまま流通
空気に吹飛ばされるいわゆる水飛びを抑制することがで
き、結露水を両端ヘッダー部分からスムーズに排出でき
るという利点がある。
In the heat exchange device shown in FIG. 1, the intake air is blown out of the casing (B) by the fan (C) after passing through the entire core (7) of the evaporator (A) evenly. During this time, the air exchanges heat with the refrigerant flowing in the tube (3) of the evaporator and is cooled. Further, as shown in the figure, since the evaporator (A) is installed so as to be substantially V-shaped with respect to the air flow direction, the following advantages are obtained. That is, dew water generated by condensation of the flowing air adheres to the surface of the tube (3), and the dew water moves in the direction of the header on both sides along the tube by the urging force of the flowing air. Therefore, there is an advantage that the so-called water splash, in which the condensed water generated in the central portion of the core portion (7) is directly blown off to the flowing air, can be suppressed, and the condensed water can be smoothly discharged from both end header portions.

さらに、屈成部(70)においてチューブ(3)および
フィン(4)が左右に分割されるとともに、このチュー
ブ(3)の分割端部が中間ヘッダー(9)に連通接続さ
れ、かつ中間ヘッダー(9)の両側のチューブ群が半チ
ューブピッチずつずれた交互配置状態で中間ヘッダー
(9)に連結されていることにより、一方のチューブ群
から流入した冷媒が一端中間ヘッダー(9)で合流さ
れ、撹拌されてから他方のチューブ群に流出することに
なり、両端にのみヘッダーが存在する場合に較べて熱交
換効率を向上できる利点がある。
Further, the tube (3) and the fin (4) are divided right and left at the bending portion (70), and the divided end of the tube (3) is connected to the intermediate header (9), and the intermediate header (9) is connected. Since the tube groups on both sides of 9) are connected to the intermediate header (9) in an alternately arranged state shifted by a half tube pitch, the refrigerant flowing from one of the tube groups is once joined by the intermediate header (9), After being stirred, it flows out to the other tube group, and there is an advantage that the heat exchange efficiency can be improved as compared with the case where headers are present only at both ends.

以上の実施例では蒸発器を略逆V字形にして空気流通
路に配置した場合を示したが、第3図に示すように、蒸
発器をその曲成部(70)が風下側となる略V形をなすよ
うに空気流通路に配設しても良い。
In the above embodiment, the case where the evaporator is arranged in the air flow passage in a substantially inverted V-shape has been shown. However, as shown in FIG. 3, the evaporator has a curved portion (70) on the leeward side. It may be arranged in the air flow passage so as to form a V shape.

なお、第3図に示す実施例において、第1図及び第2
図に示した第1実施例と同一名称部分については対応箇
所に同一符号を付してその説明を省略する。
In the embodiment shown in FIG. 3, FIG. 1 and FIG.
Corresponding parts with the same names as those in the first embodiment shown in the drawing are denoted by the same reference numerals, and description thereof will be omitted.

また、図示していないが、蒸発器は、冷媒入口管
(5)および同出口管(6)がいずれも一方のヘッダー
(1)の両端に取着されると共に、同ヘッダー(1)の
長さ方向の中間に仕切部材が設けられ、入口管(5)よ
り流入した冷媒は他方のヘッダー(2)に至ったのち、
Uターンして出口管(6)より流出するものとなされた
ものであっても良い。
Although not shown, the evaporator has a refrigerant inlet pipe (5) and an outlet pipe (6) both attached to both ends of one header (1), and the length of the header (1). A partition member is provided in the middle of the direction, and the refrigerant flowing from the inlet pipe (5) reaches the other header (2),
It may be one that makes a U-turn and flows out of the outlet pipe (6).

発明の効果 この発明に係る熱交換装置は、上述のとおり、複数本
の偏平チューブとフィンとが交互配置となされるととも
に、各チューブの両端が1対の中空ヘッダーに連通接続
された熱交換器を備え、該熱交換器がチューブの長さ方
向の中間部で略V状に曲成されるとともに、空気流通方
向に対し曲成部を風上側とする略逆V形あるいは曲成部
を風下側とする略V形をなして空気流通路に配設されて
なる熱交換装置であって、前記屈成部においてチューブ
およびフィンが分割されるとともに、このチューブの分
割端部が前記屈成部に設けられた中間ヘッダーに連通接
続されてなることを特徴とするものである。従ってま
ず、使用する熱交換器がマルチフロー型のものであるこ
とにより、それ自体拡管式の熱交換器に較べて熱交換性
能を向上することができる。かつまた、このマルチフロ
ー型の熱交換器が略V形に曲成されるとともに、空気流
通方向に対して略V形あるいは略逆V形に配設されてい
るから、直線状の熱交換器に較べて熱交換器の長さ(チ
ューブ長さ)が同じであれば少なくとも空気流通方向に
おける見掛上の長さを短縮でき、熱交換装置全体の大き
さをコンパクトにまとめることができる。しかも、ドレ
ンパンの位置を高くすることもでき、ドレン処理も容易
となしうる。一方、装置全体の大きさが同じである場合
は、熱交換器の長さ(チューブ長さ)の長い熱交換器を
収容できるから、熱交換性能の増大を図ることができ
る。
Effect of the Invention As described above, the heat exchanger according to the present invention has a heat exchanger in which a plurality of flat tubes and fins are alternately arranged and both ends of each tube are connected to a pair of hollow headers. The heat exchanger is bent in a substantially V-shape at an intermediate portion in the longitudinal direction of the tube, and a substantially inverted V-shaped portion or a leeward portion having a bent portion in the airflow direction with the bent portion on the windward side. A heat exchange device having a substantially V-shaped side and disposed in an air flow passage, wherein a tube and a fin are divided at the bending portion, and a divided end of the tube is connected to the bending portion. And is connected to an intermediate header provided in the communication device. Therefore, first, since the heat exchanger to be used is a multi-flow type, the heat exchange performance can be improved as compared with the tube-type heat exchanger itself. Further, since the multi-flow type heat exchanger is bent in a substantially V shape and is disposed in a substantially V shape or a substantially inverted V shape with respect to the air flow direction, a linear heat exchanger is provided. If the lengths of the heat exchangers (tube lengths) are the same as compared with the above, at least the apparent length in the air flow direction can be reduced, and the size of the entire heat exchange device can be reduced in size. In addition, the position of the drain pan can be raised, and the drain treatment can be facilitated. On the other hand, when the size of the entire device is the same, a heat exchanger having a long heat exchanger length (tube length) can be accommodated, so that the heat exchange performance can be increased.

その上、一方のチューブ群から流入した冷媒が一旦中
間ヘッダーで合流され、撹拌されてから他方のチューブ
群に流出することになるから、両端にのみヘッダーが存
在する場合に較べて熱交換効率が向上するという利点を
有する。
In addition, the refrigerant flowing from one of the tube groups is once merged at the intermediate header, stirred and then flows out to the other tube group, so that the heat exchange efficiency is lower than in the case where the header exists only at both ends. It has the advantage of improving.

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

第1図はこの発明の第1実施例を示す熱交換装置の正面
図、第2図は第1図の装置に用いた熱交換器の斜視図、
第3図はこの発明の第2実施例に係る熱交換装置の正面
図、第4図はV形に曲成しないマルチフロー形熱交換器
を用いた熱交換装置の正面図、第5図は第4図の装置に
用いた熱交換器とファンを示す斜視図である。 (1)(2)……ヘッダー、(3)……偏平チューブ、
(4)……フィン、(7)……コア部、(70)……曲成
部、(9)……中間ヘッダー
FIG. 1 is a front view of a heat exchanger showing a first embodiment of the present invention, FIG. 2 is a perspective view of a heat exchanger used in the apparatus of FIG.
FIG. 3 is a front view of a heat exchange device according to a second embodiment of the present invention, FIG. 4 is a front view of a heat exchange device using a multi-flow type heat exchanger that is not bent into a V shape, and FIG. FIG. 5 is a perspective view showing a heat exchanger and a fan used in the apparatus of FIG. (1) (2) ... header, (3) ... flat tube,
(4) fin, (7) core part, (70) composed part, (9) intermediate header

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F28D 1/00 - 9/04 F24F 1/00 - 1/02 F25B 39/00 - 39/04 F28F 9/00 - 9/26 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) F28D 1/00-9/04 F24F 1/00-1/02 F25B 39/00-39/04 F28F 9 / 00-9/26

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】複数本の偏平チューブ(3)とフィン
(4)とが交互配置となされるとともに、各チューブ
(3)の両端が1対の中空ヘッダー(1)(2)に連通
接続された熱交換器(A)を備え、 該熱交換器(A)がチューブ(3)の長さ方向の中間部
で略V状に曲成されるとともに、空気流通方向に対し曲
成部(70)を風上側とする略逆V形あるいは曲成部を風
下側とする略V形をなして空気流通路に配設されてなる
熱交換装置であって、 前記屈成部(70)においてチューブ(3)およびフィン
(4)が分割されるとともに、このチューブ(3)の分
割端部が前記屈成部に設けられた中間ヘッダー(9)に
連通接続されてなることを特徴とする熱交換装置。
A plurality of flat tubes (3) and fins (4) are alternately arranged, and both ends of each tube (3) are connected to a pair of hollow headers (1) and (2). The heat exchanger (A) is bent in a substantially V-shape at an intermediate portion in the longitudinal direction of the tube (3), and the bent portion (70) is formed in the air flow direction. A heat exchange device is provided in the air flow passage in a substantially inverted V-shape having a windward side or a substantially V-shaped shape having a bent portion on the leeward side, wherein a tube is provided at the bent portion (70). (3) The fin (4) is divided, and the divided end of the tube (3) is connected to an intermediate header (9) provided in the bent portion, and the heat exchange is performed. apparatus.
JP2318366A 1990-11-22 1990-11-22 Heat exchange equipment Expired - Lifetime JP3043051B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2318366A JP3043051B2 (en) 1990-11-22 1990-11-22 Heat exchange equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2318366A JP3043051B2 (en) 1990-11-22 1990-11-22 Heat exchange equipment

Publications (2)

Publication Number Publication Date
JPH04187990A JPH04187990A (en) 1992-07-06
JP3043051B2 true JP3043051B2 (en) 2000-05-22

Family

ID=18098348

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2318366A Expired - Lifetime JP3043051B2 (en) 1990-11-22 1990-11-22 Heat exchange equipment

Country Status (1)

Country Link
JP (1) JP3043051B2 (en)

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