JPH0626777A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPH0626777A JPH0626777A JP18387192A JP18387192A JPH0626777A JP H0626777 A JPH0626777 A JP H0626777A JP 18387192 A JP18387192 A JP 18387192A JP 18387192 A JP18387192 A JP 18387192A JP H0626777 A JPH0626777 A JP H0626777A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- heat transfer
- heat
- transfer tubes
- heat exchange
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-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
- F28D1/02—Heat-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
- F28D1/04—Heat-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
- F28D1/047—Heat-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
- F28D1/0477—Heat-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 being bent in a serpentine or zig-zag
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/122—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and being formed of wires
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
- F28F9/262—Arrangements 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)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本願発明は、多数平行に配置され
た伝熱管の外周に対してその管軸と平行に多数の網目状
フィンを接合してなるメッシュフィンタイプの熱交換器
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mesh fin type heat exchanger in which a large number of mesh fins are joined to the outer circumference of a plurality of heat transfer tubes arranged in parallel with each other in parallel to the tube axis. is there.
【０００２】[0002]
【従来の技術】空気調和機用として使用される熱交換器
としては、多数平行に配置した伝熱管に対して直交する
多数の板状フィンを配置してなるクロスフィンタイプの
熱交換器が良く知られている。このような構成の熱交換
器において、空気流通方向に伝熱管を複数列配置する場
合、板状フィンに伝熱管を直交させるためには、全ての
伝熱管を平行にしなければならないが、上流側に配列さ
れる伝熱管の後方に形成される死水域に下流側の伝熱管
が配列されると、下流側の伝熱管における熱伝達が低下
するおそれがある。そこで、クロスフィンタイプの熱交
換器の場合、上流側に配列される伝達管の死水域の影響
を下流側に配列される伝達管が受けないように、伝熱管
配列を空気流通方向に関して千鳥配列とすることが行な
われている。しかしながら、クロスフィンタイプの熱交
換器の場合、板状フィンに対して伝熱管を直交状に挿通
する構成とされているため、熱交換性能を保持しつつ熱
交換器を小型化するには限界があった。2. Description of the Related Art As a heat exchanger used for an air conditioner, a cross fin type heat exchanger in which a large number of plate-shaped fins orthogonal to a plurality of heat transfer tubes arranged in parallel are arranged is often used. Are known. In a heat exchanger having such a configuration, when arranging a plurality of rows of heat transfer tubes in the air flow direction, in order to make the heat transfer tubes orthogonal to the plate fins, all the heat transfer tubes must be parallel, but the upstream side When the heat transfer tubes on the downstream side are arranged in the dead water region formed behind the heat transfer tubes arranged on the lower side, heat transfer in the heat transfer tubes on the downstream side may be reduced. Therefore, in the case of a cross-fin type heat exchanger, the heat transfer tube arrangement is arranged in a staggered arrangement in the air flow direction so that the transfer tubes arranged on the downstream side are not affected by the dead water area of the transfer tubes arranged on the upstream side. Is being done. However, in the case of the cross-fin type heat exchanger, the heat transfer tubes are inserted orthogonally to the plate-shaped fins, so there is a limit to downsizing the heat exchanger while maintaining heat exchange performance. was there.
【０００３】一方、近年熱交換性能を保持しつつ熱交換
器の小型化を図ることが機器の有効利用を図る観点から
求められるようになっており、多数平行に配置された伝
熱管の外周に対してその管軸と平行に多数の網目状フィ
ンを接合してなるメッシュフィンタイプの熱交換器の開
発が進められている(例えば、実開昭６１ー１９２１８
５号公報参照)。On the other hand, in recent years, it has been required to reduce the size of the heat exchanger while maintaining the heat exchange performance, from the viewpoint of effectively utilizing the equipment, and a large number of heat transfer tubes are arranged on the outer circumference of the heat transfer tubes arranged in parallel. On the other hand, the development of a mesh fin type heat exchanger in which a large number of mesh fins are joined in parallel with the tube axis is underway (for example, in Japanese Utility Model Publication 61-19218).
(See Japanese Patent Publication No. 5).
【０００４】[0004]
【発明が解決しようとする課題】ところで、メッシュフ
ィンタイプの熱交換器の場合、多数平行に配置された伝
熱管の外周に対してその管軸と平行に多数の網目状フィ
ンを接合してなる単一モジュール(即ち、熱交モジュー
ル)を複数枚重合することにより小型化された多列熱交
換器を形成することができるが、単に、複数枚の熱交モ
ジュールを重合しただけでは、上述したように上流側の
熱交モジュールにおける伝熱管の後方に生ずる死水域の
影響を下流側の熱交モジュールにおける伝熱管およびフ
ィンが受けることとなって、必ずしも熱交換性能が向上
しない場合がある。By the way, in the case of a mesh fin type heat exchanger, a large number of mesh fins are joined to the outer periphery of a plurality of heat transfer tubes arranged in parallel to each other in parallel to the tube axis. Although it is possible to form a miniaturized multi-row heat exchanger by polymerizing a plurality of single modules (i.e., heat exchange modules), it is necessary to simply polymerize a plurality of heat exchange modules as described above. As described above, the dead water region generated behind the heat transfer tube in the upstream heat exchange module is affected by the heat transfer tube and the fins in the downstream heat exchange module, and the heat exchange performance may not necessarily be improved.
【０００５】本願発明は、上記の点に鑑みてなされたも
ので、空気流通方向に関して下流側に配列された熱交モ
ジュールの熱伝達率の向上を図るとともに、複数列熱交
換器のコンパクト化を図ることを目的とするものであ
る。The present invention has been made in view of the above points, and aims to improve the heat transfer coefficient of a heat exchange module arranged on the downstream side with respect to the air flow direction and to make a multiple row heat exchanger compact. This is intended to be achieved.
【０００６】[0006]
【課題を解決するための手段】請求項１の発明では、上
記課題を解決するための手段として、図面に示すよう
に、多数平行に配置された伝熱管１,１・・と該伝熱管
１,１・・の外周に対してその管軸と平行に接合された
多数の網目状フィン２,２・・とによって熱交モジュー
ルＡを構成し、複数枚の熱交モジュールＡ,Ａ・・を前
記網目状フィン２が隣合うように重合してなる熱交換器
において、隣合う熱交モジュールＡ,Ａにおける伝熱管
配設方向を交差させている。In the invention of claim 1, as a means for solving the above-mentioned problems, as shown in the drawings, a large number of heat transfer tubes 1, 1, ... The heat exchange module A is composed of a large number of mesh fins 2,2 ... Connected to the outer circumference of the heat exchanger module 1 ... In the heat exchanger in which the mesh fins 2 are superposed so as to be adjacent to each other, the heat transfer tube disposition directions of the adjacent heat exchange modules A and A are crossed.
【０００７】請求項２の発明では、上記課題を解決する
ための手段として、図面に示すように、前記請求項１記
載の熱交換器において、隣合う熱交モジュールＡ,Ａに
おける伝熱管配設方向を直交させるとともに、奇数列お
よび偶数列の熱交モジュールＡ,Ａ・・における伝熱管
１,１・・を、空気流通方向に直交する方向に位相差を
以って配列している。According to the invention of claim 2, as a means for solving the above-mentioned problems, as shown in the drawings, in the heat exchanger according to claim 1, the heat transfer tubes are arranged in adjacent heat exchange modules A, A. The heat transfer tubes 1, 1, ... In the heat exchange modules A, A ... Of the odd-numbered rows and the even-numbered rows are arranged with a phase difference in the direction orthogonal to the air circulation direction while making the directions orthogonal to each other.
【０００８】[0008]
【作用】請求項１の発明では、上記手段によって次のよ
うな作用が得られる。According to the first aspect of the invention, the following actions can be obtained by the above means.
【０００９】即ち、隣合う熱交モジュールＡ,Ａにおけ
る伝熱管配設方向を交差させた場合、空気流通方向に関
して上流側に配列された伝熱管１,１・・の死水域の影
響を下流側に配列された伝熱管１,１・・および網目状
フィン２,２・・が受けにくくなる。また、直交する管
列の熱伝達率が単管の場合よりも高い値を示すという報
告[例えば、第２８回日本伝熱シンポジウム講演論文集
Ｐ４９〜５１(Ａ１４２直交二円柱よりの強制対流熱
伝達)参照]があるように、熱交換器全体としての効率も
向上することとなる。さらに、従来のクロスフィンタイ
プのものと異なって、熱交モジュールＡ,Ａ・・を密着
重合しても、ほとんど熱交換性能の低下が見られない。That is, when the heat transfer tube arrangement directions in the adjacent heat exchange modules A, A are crossed, the influence of the dead water area of the heat transfer tubes 1, 1, ... The heat transfer tubes 1, 1 ... And the mesh fins 2, 2 ,. In addition, it is reported that the heat transfer coefficient of the orthogonal tube rows is higher than that of the single tube [for example, Proceedings of the 28th Japan Heat Transfer Symposium P49-51 (A142 Forced convection heat transfer from two orthogonal cylinders). ) Reference], the efficiency of the heat exchanger as a whole will be improved. Further, unlike the conventional cross fin type, even if the heat exchange modules A, A ... Are contact-polymerized, the heat exchange performance is hardly deteriorated.
【００１０】請求項２の発明では、上記手段によって次
のような作用が得られる。According to the second aspect of the invention, the following effects can be obtained by the above means.
【００１１】即ち、奇数列同士あるいは偶数列同士の伝
熱管１,１・・が位相差を以って配列されているため、
空気流通方向に関して上流側に配列された伝熱管１,１
・・の死水域の影響が２列下流側に配列された伝熱管
１,１・・(両伝熱管は平行となっている)および網目状
フィン２,２・・に及ぶことがなくなる。That is, since the heat transfer tubes 1, 1, ... Of odd rows or even rows are arranged with a phase difference,
Heat transfer tubes 1, 1 arranged upstream in the direction of air flow
The influence of the dead water area on the heat transfer tubes 1,1 ... (both heat transfer tubes are parallel) and the mesh fins 2,2 ..
【００１２】[0012]
【発明の効果】請求項１の発明によれば、多数平行に配
置された伝熱管１,１・・と該伝熱管１,１・・の外周に
対してその管軸と平行に接合された多数の網目状フィン
２,２・・とによって熱交モジュールＡを構成し、複数
枚の熱交モジュールＡ,Ａ・・を前記網目状フィン２が
隣合うように重合してなる熱交換器において、隣合う熱
交モジュールＡ,Ａにおける伝熱管配設方向を交差させ
て、空気流通方向に関して上流側に配列された伝熱管
１,１・・の死水域の影響を下流側に配列された伝熱管
１,１・・および網目状フィン２,２・・が受けにくくな
るようにし、且つ交差配列とされた複数列配管による熱
伝達率の向上を図り得るようにしたので、熱交換器全体
としての効率向上を達成できるという優れた効果があ
る。また、従来のクロスフィンタイプのものと異なっ
て、熱交モジュールＡ,Ａ・・を密着重合しても、ほと
んど熱交換性能の低下が見られないので、複数列熱交換
器のコンパクト化に大いに寄与するという効果もある。According to the first aspect of the present invention, a large number of heat transfer tubes 1, 1 ... Arranged in parallel and the outer circumferences of the heat transfer tubes 1, 1. A heat exchanger in which a heat exchange module A is composed of a large number of mesh fins 2, 2, ... And a plurality of heat exchange modules A, A. , The heat transfer tubes in the adjacent heat exchange modules A, A are crossed, and the influence of the dead water area of the heat transfer tubes 1, 1 ... Arranged on the upstream side in the air circulation direction is transferred on the downstream side. Since the heat pipes 1, 1 ..., And the mesh fins 2, 2 ... Are made hard to receive, and the heat transfer coefficient can be improved by the multiple rows of pipes that are arranged in an intersecting arrangement, the heat exchanger as a whole There is an excellent effect that the efficiency improvement can be achieved. Also, unlike the conventional cross fin type, even if the heat exchange modules A, A ... Are contact-polymerized, almost no deterioration in heat exchange performance is observed, so it is possible to make the multi-row heat exchanger compact. There is also an effect of contributing.
【００１３】請求項２の発明によれば、請求項１記載の
熱交換器において、隣合う熱交モジュールＡ,Ａにおけ
る伝熱管配設方向を直交させるとともに、奇数列および
偶数列の熱交モジュールＡ,Ａ・・における伝熱管１,１
・・を、空気流通方向に直交する方向に位相差を以って
配列して、空気流通方向に関して上流側に配列された伝
熱管１,１・・の死水域の影響が２列下流側に配列され
た伝熱管１,１・・(両伝熱管は平行となっている)およ
び網目状フィン２,２・・に及ぶことがなくなるように
したので、熱交換器全体としての効率向上がより効果的
となるとともに、より一層のコンパクト化も図れるとい
う優れた効果がある。According to the second aspect of the present invention, in the heat exchanger according to the first aspect, the heat transfer tubes are arranged in adjacent heat exchange modules A and A at right angles, and the heat exchange modules in odd rows and even rows are arranged. Heat transfer tubes in A, A ...
.. are arranged with a phase difference in the direction orthogonal to the air flow direction, and the influence of the dead water region of the heat transfer tubes 1, 1 ... Since the arranged heat transfer tubes 1,1 ... (both heat transfer tubes are parallel) and the mesh fins 2,2 ... are prevented from extending, the efficiency of the heat exchanger as a whole is improved. In addition to being effective, there is an excellent effect that further downsizing can be achieved.
【００１４】[0014]
【実施例】以下、添付の図面を参照して本願発明の幾つ
かの好適な実施例を説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Some preferred embodiments of the present invention will be described below with reference to the accompanying drawings.
【００１５】実施例１ 図１ないし図３には、本願発明の実施例１にかかる熱交
換器が示されている。本実施例は、請求項１の発明に対
応するものである。Embodiment 1 FIGS. 1 to 3 show a heat exchanger according to Embodiment 1 of the present invention. The present embodiment corresponds to the invention of claim 1.
【００１６】本実施例の熱交換器は、多数平行に配置さ
れた伝熱管１,１・・と該伝熱管１,１・・の外周に対し
てその管軸と平行に接合された多数(本実施例の場合、
６枚)の網目状フィン２,２・・とによって熱交モジュー
ルＡを構成し、複数枚(本実施例の場合、４枚)の熱交モ
ジュールＡ,Ａ・・を前記網目状フィン２が隣合うよう
に重合して構成されており、隣合う熱交モジュールＡ,
Ａにおける伝熱管配設方向は直交せしめられている。な
お、この熱交換器においては、伝熱管１,１・・内を流
通する冷媒と、網目状フィン２,２・・に直交する方向
に流通する空気流Ｆとの間で熱交換が行なわれることと
なっている。In the heat exchanger of this embodiment, a large number of heat transfer tubes 1, 1, ... Arranged in parallel and a large number (joined to the outer circumferences of the heat transfer tubes 1, 1 ,. In the case of this embodiment,
The heat exchange module A is composed of six (6) mesh fins 2, 2, ... And a plurality of heat exchanger modules A, A ... Adjacent heat exchange modules A, which are constructed by superimposing them next to each other,
The heat transfer tube arrangement direction in A is orthogonal to each other. In this heat exchanger, heat is exchanged between the refrigerant flowing in the heat transfer tubes 1, 1, ... And the air flow F flowing in the direction orthogonal to the mesh fins 2, 2. It is supposed to be.
【００１７】前記熱交モジュールＡにおける網目状フィ
ン２には、図２および図３に示すように、伝熱管１,１
・・との接合部において伝熱管１,１・・の外周に密着
し得るトンネル状の湾曲部２a,２a・・が形成されてい
る。なお、熱交モジュールＡにおける網目状フィン２,
２・・の湾曲部２a,２a・・は、最内側のものが深く、
外側に向かうに従って浅くされており、最外側の網目状
フィン２と伝熱管１との接合部は平担面とされている。
そして、熱交モジュールＡにおける伝熱管１と湾曲部２
a,２a・・との接合は、ハンダ付等の適宜固着手段によ
り固着されることとなっている。As shown in FIGS. 2 and 3, the mesh fins 2 in the heat exchange module A have heat transfer tubes 1, 1 as shown in FIGS.
At the joint portion with .., tunnel-like curved portions 2a, 2a .. In addition, the mesh fins 2 in the heat exchange module A,
The innermost one of the curved portions 2a, 2a ... of 2 ...
It becomes shallower toward the outside, and the joint between the outermost mesh fin 2 and the heat transfer tube 1 is a flat surface.
Then, the heat transfer tube 1 and the bending portion 2 in the heat exchange module A
The connection with a, 2a ... Is to be fixed by appropriate fixing means such as soldering.
【００１８】しかして、本実施例の熱交換器において
は、各熱交モジュールＡにおける伝熱管１,１・・同士
はＵ字状接続管３,３・・を介して接続されており、熱
交モジュールＡ,Ａ・・相互は連絡管４,４・・を介して
接続されている。従って、本実施例の熱交換器において
は、熱媒体(例えば、水、ブライン、冷媒等)Ｘは、図１
に矢印Ｘで示すように熱交モジュールＡ,Ａ・・を１パ
スで連続的に流れることとなっている。なお、各熱交モ
ジュールＡにおける伝熱管１,１・・の管端を接続する
ヘッダーを設け、ヘッダー相互を連絡管を介して接続す
るようにして複数パスとする場合もある。In the heat exchanger of this embodiment, however, the heat transfer tubes 1, 1 ... In each heat exchange module A are connected to each other through the U-shaped connecting tubes 3, 3 ,. The exchange modules A, A ... Are connected to each other via the connecting pipes 4, 4. Therefore, in the heat exchanger of this embodiment, the heat medium (for example, water, brine, refrigerant, etc.) X is
As shown by the arrow X, the heat exchange modules A, A ... Are continuously flowed in one pass. In some cases, a header for connecting the tube ends of the heat transfer tubes 1, 1, ... In each heat exchange module A is provided, and the headers are connected to each other through a connecting tube to form a plurality of paths.
【００１９】上記のように構成したことにより、本実施
例の熱交換器では次のような作用が得られる。With the above construction, the heat exchanger of this embodiment can obtain the following effects.
【００２０】隣合う熱交モジュールＡ,Ａにおける伝熱
管配設方向を直交させた場合、空気流通方向に関して上
流側に配列された伝熱管１,１・・の死水域の影響を下
流側に配列された伝熱管１,１・・および網目状フィン
２,２・・が受けにくくなって熱伝達率の向上が図れる
とともに、直交する管列の熱伝達率が単管の場合よりも
高い値を示すという報告[例えば、第２８回日本伝熱シ
ンポジウム講演論文集Ｐ４９〜５１(Ａ１４２ 直交二
円柱よりの強制対流熱伝達)参照]があるように、熱交換
器全体としての効率も向上することとなる。さらに、従
来のクロスフィンタイプのものと異なって、熱交モジュ
ールＡ,Ａ・・を密着重合しても、ほとんど熱交換性能
の低下が見られないところから、複数列熱交換器のコン
パクト化も図れる。When the heat transfer tubes are arranged adjacent to each other in the heat exchange modules A and A, the influence of the dead water area of the heat transfer tubes 1, 1 ... Arranged on the upstream side in the air flow direction is arranged on the downstream side. The heat transfer tubes 1, 1, ... And the mesh fins 2, 2, .. Are less likely to be received, and the heat transfer coefficient can be improved, and the heat transfer coefficient of the orthogonal tube rows is higher than that of the single tube. As shown in the report [see, for example, Proceedings of the 28th Japan Heat Transfer Symposium P49-51 (A142 Forced convection heat transfer from two orthogonal cylinders)], the efficiency of the heat exchanger as a whole is improved. Become. Furthermore, unlike the conventional cross fin type, even if the heat exchange modules A, A ... Are contact-polymerized, almost no deterioration in heat exchange performance is observed, so the multi-row heat exchanger can be made compact. Can be achieved.
【００２１】なお、本実施例では、隣合う熱交モジュー
ルＡ,Ａにおける伝熱管配設方向の交差角度が直角とな
るようにしているが、伝熱管配設方向の交差角度を、直
角以外の角度としても本実施例の同様な作用効果を期待
できることは勿論である。In the present embodiment, the intersecting angles of the heat transfer tube arranging directions of the adjacent heat exchange modules A, A are set to be a right angle, but the intersecting angle of the heat transfer tube arranging direction is not a right angle. It is needless to say that the same action and effect of this embodiment can be expected as the angle.
【００２２】実施例２ 図４ないし図６には、本願発明の実施例２にかかる熱交
換器が示されている。本実施例は、請求項１および２の
発明に対応するものである。Embodiment 2 FIGS. 4 to 6 show a heat exchanger according to Embodiment 2 of the present invention. The present embodiment corresponds to the inventions of claims 1 and 2.
【００２３】本実施例の場合、奇数列および偶数列の熱
交モジュールＡ,Ａ・・における伝熱管１,１・・は、空
気流通方向に直交する方向に位相差(本実施例の場合、
約６０°)をもって配列されている。つまり、熱交換器
全体として見ると、伝熱管１,１・・が、空気流通方向
に関して千鳥配列とされているのである。In the case of this embodiment, the heat transfer tubes 1, 1, ... In the heat exchange modules A, A ..
They are arranged at about 60 °. In other words, when viewed as a whole heat exchanger, the heat transfer tubes 1, 1, ... Are staggered in the air flow direction.
【００２４】このように構成すると、空気流通方向に関
して上流側に配列された伝熱管１，１・・の死水域の影
響が２列下流側に配列された伝熱管１，１・・(両伝熱
管は平行となっている)および網目状フィン２,２・・に
及ぶことがなくなり、熱交換器全体としての効率向上が
より効果的となるとともに、より一層のコンパクト化も
図れる。その他の構成および作用効果は実施例１と同様
なので説明を省略する。According to this structure, the influence of the dead water area of the heat transfer tubes 1, 1 ... Arranged on the upstream side in the air flow direction is arranged in two rows on the heat transfer tubes 1, 1. Since the heat pipes are parallel to each other and the mesh fins 2, 2, ... Are not provided, the efficiency of the heat exchanger as a whole is improved more effectively and the size can be further reduced. Other configurations, functions, and effects are similar to those of the first embodiment, and therefore description thereof will be omitted.
【００２５】実施例３ 図７および図８には、本願発明の実施例３にかかる熱交
換器が示されている。本実施例は、請求項１および２の
発明に対応するものである。Embodiment 3 FIGS. 7 and 8 show a heat exchanger according to Embodiment 3 of the present invention. The present embodiment corresponds to the inventions of claims 1 and 2.
【００２６】本実施例の場合、隣合う熱交モジュール
Ａ,Ａにおける伝熱管配設方向は約６０°の位相差をも
って交差せしめられている。また、奇数列および偶数列
の熱交モジュールＡ,Ａ・・における伝熱管１,１・・
は、空気流通方向に直交する方向に位相差(本実施例の
場合、約６０°)をもって配列されている。つまり、図
８に示すように、１列目および３列目の熱交モジュール
Ａの伝熱管１Ａ,１Ａ・・および１Ｃ,１Ｃ・・(実線図
示および鎖線図示)と、２列目の熱交モジュールＡの伝
熱管１Ｂ,１Ｂ・・(点線図示)とが約６０°の位相差を
以って交差せしめられ、且つ１列目の熱交モジュールＡ
の伝熱管１Ａ,１Ａ・・(実線図示)と、３列目の熱交モ
ジュールＡの伝熱管１Ｃ,１Ｃ・・(鎖線図示)とが空気
流通方向に直交する方向に位相差(本実施例の場合、約
６０°)をもって配列されているのである。その他の構
成は実施例２と同様なので説明を省略する。In the case of this embodiment, the heat transfer tube arrangement directions in the adjacent heat exchange modules A, A are crossed with a phase difference of about 60 °. In addition, the heat transfer tubes 1, 1, ... In the heat exchange modules A, A.
Are arranged with a phase difference (about 60 ° in this embodiment) in the direction orthogonal to the air flow direction. That is, as shown in FIG. 8, the heat transfer tubes 1A, 1A ... And 1C, 1C .. (solid lines and chain lines) of the heat exchange module A in the first and third rows and the heat exchange tubes in the second row are shown. The heat transfer tubes 1B, 1B (shown by dotted lines) of the module A are crossed with a phase difference of about 60 °, and the heat exchange module A in the first row
The heat transfer tubes 1A, 1A .. (shown by solid lines) and the heat transfer tubes 1C, 1C .. (shown by chain lines) of the third-row heat exchange module A have a phase difference in the direction orthogonal to the air flow direction (this embodiment). In this case, they are arranged at about 60 °). The other configuration is similar to that of the second embodiment, and thus the description is omitted.
【００２７】このように構成したことにより、蒸発器と
して使用した場合に、傾斜した伝熱管１,１・・に沿っ
てドレン水が良好に排出されることとなり、通風抵抗の
減少に寄与する。その他の作用効果は実施例２と同様で
ある。With this configuration, when used as an evaporator, drain water is discharged well along the inclined heat transfer tubes 1, 1, ..., which contributes to reduction of ventilation resistance. Other functions and effects are similar to those of the second embodiment.
【００２８】本願発明は、上記各実施例の構成に限定さ
れるものではなく、発明の要旨を逸脱しない範囲におい
て適宜設計変更可能なことは勿論である。The invention of the present application is not limited to the configuration of each of the above-described embodiments, and it goes without saying that the design can be appropriately changed without departing from the scope of the invention.
【図１】本願発明の実施例１にかかる熱交換器の分解斜
視図である。FIG. 1 is an exploded perspective view of a heat exchanger according to a first embodiment of the present invention.
【図２】本願発明の実施例１にかかる熱交換器の拡大側
面図である。FIG. 2 is an enlarged side view of the heat exchanger according to the first embodiment of the present invention.
【図３】本願発明の実施例１にかかる熱交換器の拡大平
面図である。FIG. 3 is an enlarged plan view of the heat exchanger according to the first embodiment of the present invention.
【図４】本願発明の実施例２にかかる熱交換器の分解斜
視図である。FIG. 4 is an exploded perspective view of a heat exchanger according to a second embodiment of the present invention.
【図５】本願発明の実施例２にかかる熱交換器の拡大側
面図である。FIG. 5 is an enlarged side view of the heat exchanger according to the second embodiment of the present invention.
【図６】本願発明の実施例２にかかる熱交換器の拡大平
面図である。FIG. 6 is an enlarged plan view of the heat exchanger according to the second embodiment of the present invention.
【図７】本願発明の実施例３にかかる熱交換器の分解斜
視図である。FIG. 7 is an exploded perspective view of a heat exchanger according to a third embodiment of the present invention.
【図８】本願発明の実施例３にかかる熱交換器における
伝熱管配列を示す模式図である。FIG. 8 is a schematic diagram showing an arrangement of heat transfer tubes in a heat exchanger according to a third embodiment of the present invention.
１は伝熱管、２は網目状フィン、Ａは熱交モジュール。 1 is a heat transfer tube, 2 is a mesh fin, and A is a heat exchange module.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 安尾 晃一 大阪府堺市金岡町1304番地 ダイキン工業 株式会社堺製作所金岡工場内 (72)発明者 末広 賢一 大阪府堺市金岡町1304番地 ダイキン工業 株式会社堺製作所金岡工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Koichi Yaseo 1304 Kanaoka-machi, Sakai City, Osaka Prefecture Daikin Industries, Ltd.Kanaoka Plant, Sakai Manufacturing Co., Ltd. (72) Kenichi Suehiro 1304 Kanaoka-machi, Sakai City, Osaka Prefecture Sakai Factory Kanaoka Factory
Claims (2)
・・と該伝熱管(１),(１)・・の外周に対してその管軸
と平行に接合された多数の網目状フィン(２),(２)・・
とによって熱交モジュール(Ａ)を構成し、複数枚の熱交
モジュール(Ａ),(Ａ)・・を前記網目状フィン(２)が隣
合うように重合してなる熱交換器であって、隣合う熱交
モジュール(Ａ),(Ａ)における伝熱管配設方向を交差さ
せたことを特徴とする熱交換器。1. A plurality of heat transfer tubes (1), (1) arranged in parallel.
.. and a large number of mesh fins (2), (2) joined to the outer circumference of the heat transfer tubes (1), (1) ..
A heat exchanger comprising a heat exchange module (A) composed of and a plurality of heat exchange modules (A), (A), ... A heat exchanger characterized in that the heat transfer tube disposition directions in adjacent heat exchange modules (A) and (A) are crossed.
る伝熱管配設方向を直交させるとともに、奇数列および
偶数列の熱交モジュール(Ａ),(Ａ)・・における伝熱管
(１),(１)・・を、空気流通方向に直交する方向に位相
差を以って配列したことを特徴とする前記請求項１記載
の熱交換器。2. The heat transfer tubes in the heat exchange modules (A), (A), ...
The heat exchanger according to claim 1, wherein (1), (1), ... Are arranged with a phase difference in a direction orthogonal to the air flow direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18387192A JPH0626777A (en) | 1992-07-10 | 1992-07-10 | Heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18387192A JPH0626777A (en) | 1992-07-10 | 1992-07-10 | Heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0626777A true JPH0626777A (en) | 1994-02-04 |
Family
ID=16143290
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18387192A Pending JPH0626777A (en) | 1992-07-10 | 1992-07-10 | Heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0626777A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007062916A1 (en) * | 2005-11-30 | 2007-06-07 | BSH Bosch und Siemens Hausgeräte GmbH | Refrigerant condenser for a refrigeration device |
| CN114413657A (en) * | 2021-12-23 | 2022-04-29 | 合肥通用机械研究院有限公司 | Matrix type high-temperature gas cooler |
| JP2023508434A (en) * | 2019-12-24 | 2023-03-02 | ドホ ホ | Marine fuel heating system |
-
1992
- 1992-07-10 JP JP18387192A patent/JPH0626777A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007062916A1 (en) * | 2005-11-30 | 2007-06-07 | BSH Bosch und Siemens Hausgeräte GmbH | Refrigerant condenser for a refrigeration device |
| JP2023508434A (en) * | 2019-12-24 | 2023-03-02 | ドホ ホ | Marine fuel heating system |
| CN114413657A (en) * | 2021-12-23 | 2022-04-29 | 合肥通用机械研究院有限公司 | Matrix type high-temperature gas cooler |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR0132297B1 (en) | Evaporator with a function of a condensate collector | |
| JP4989979B2 (en) | Heat exchanger | |
| JP4946348B2 (en) | Air heat exchanger | |
| JPH11294984A (en) | Juxtaposed integrated heat exchanger | |
| JP7372761B2 (en) | Heat exchanger and air conditioning system | |
| JP2002243381A (en) | Air heat exchanger and its manufacturing method | |
| JP2020094791A5 (en) | ||
| JPH04187991A (en) | Heat exchanger | |
| US3217798A (en) | Heat exchanger | |
| JPH11294973A (en) | Heat exchanger of absorption water cooler/heater | |
| JPH06174393A (en) | Heat exchanger | |
| RU2194926C2 (en) | Plate heat exchanger with corrugated plates | |
| JP2006084078A (en) | Thin heat transfer tube unit of thin multitubular heat exchanger | |
| JPH0626777A (en) | Heat exchanger | |
| JP2007505282A (en) | Heat exchanger | |
| JP3446427B2 (en) | Heat exchanger | |
| JP2002181487A (en) | Heat exchanger for air conditioner | |
| JP2007183062A (en) | Heat exchanger | |
| JPH10153393A (en) | Flat heating pipes for heat exchanger | |
| JP4184110B2 (en) | Finned tube heat exchanger | |
| JPH07324884A (en) | Corrugated fin for heat exchanger | |
| JPH03279763A (en) | Multiple heat exchanger | |
| JP2002195774A (en) | Air heat exchanger | |
| JPH03169482A (en) | Manufacture of heat exchanger | |
| JP2002350078A (en) | Heat exchanger |