JP2003269880A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JP2003269880A
JP2003269880A JP2002075386A JP2002075386A JP2003269880A JP 2003269880 A JP2003269880 A JP 2003269880A JP 2002075386 A JP2002075386 A JP 2002075386A JP 2002075386 A JP2002075386 A JP 2002075386A JP 2003269880 A JP2003269880 A JP 2003269880A
Authority
JP
Japan
Prior art keywords
heat exchanger
refrigerant pipe
parallel
fins
refrigerant
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.)
Withdrawn
Application number
JP2002075386A
Other languages
Japanese (ja)
Inventor
Hidekazu Takahashi
英一 高橋
Terukazu Ishioka
輝一 石岡
Takeshi Kubota
剛 久保田
Toshiyuki Amimoto
俊之 網本
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP2002075386A priority Critical patent/JP2003269880A/en
Publication of JP2003269880A publication Critical patent/JP2003269880A/en
Withdrawn legal-status Critical Current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
    • F28D1/047Heat-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
    • F28D1/0477Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular 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
    • F28F1/24Tubular 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 extending transversely

Abstract

<P>PROBLEM TO BE SOLVED: To provide a heat exchanger with the minimum number of joints and a high degree of design freedom while maintaining conventional heat exchanging performance combining the advantages of reliability in airtightness and refrigerant leakage resistance, heat transfer performance and the high degree of design freedom. <P>SOLUTION: In the cross fin type heat exchanger, only one refrigerant pipe is brought into contact with one independent fin. It is structured to joint the fin to one refrigerant pipe which is originally linear, and to perform planar or three-dimensional bending work the optional number of times to have an optional length. A bent part is composed of a combination of the same minimum bend radius and an optional micro linear part. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明の熱交換器構造は、冷
媒管とフィンとを組合せた構造のクロスフィン型熱交換
器に係わり、特にロー付け等による冷媒管同士の接合を
極力抑えた一筆書き構造の冷媒配管を有する熱交換器に
関し、また特にはそれを用いた冷蔵庫に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The heat exchanger structure of the present invention relates to a cross fin type heat exchanger having a structure in which refrigerant pipes and fins are combined, and particularly, it is possible to suppress joining of refrigerant pipes by brazing as much as possible. The present invention relates to a heat exchanger having a writing-structured refrigerant pipe, and more particularly to a refrigerator using the heat exchanger.

【0002】[0002]

【従来の技術】冷媒管とフィンとを組合せた構造の従来
のクロスフィン型熱交換器は、社団法人日本塑性加工学
会編「チューブフォーミング」(初版、1992年、コ
ロナ社)第63頁に記載のように、一定間隔で平行に配
列された複数の冷媒管と、その冷媒管に垂直な方向に一
定間隔で並べられた複数枚のフィンで構成されている。
この時、1枚の独立したフィンには、複数個の通孔が設
けられており、その各通孔中に冷媒管が通され、通孔中
の各々の冷媒管内部にその内径よりも外径がわずかに大
きな拡管用マンドレルを圧入することによってそれぞれ
のフィンと冷媒管を締結させている。また冷媒管同士
は、別工程で180度に曲げ加工された個別部品を用い
てろう付け等で接合されており、直管と180度曲げ管
とを交互に接合して熱交換器を構成する。フィンは必要
に応じてスリットを設けて熱交換性能を増大させる方策
も採られている。
2. Description of the Related Art A conventional cross fin type heat exchanger having a structure in which a refrigerant pipe and fins are combined is described in "Tube Forming" (First Edition, 1992, Corona Publishing Co., Ltd.), p. 63, edited by the Japan Society for Plasticity Processing. As described above, it is composed of a plurality of refrigerant tubes arranged in parallel at regular intervals and a plurality of fins arranged at regular intervals in a direction perpendicular to the refrigerant tubes.
At this time, one independent fin is provided with a plurality of through holes, a refrigerant pipe is passed through each of the through holes, and the inside of each refrigerant pipe in the through hole is outside the inner diameter thereof. The fins and the refrigerant pipes are fastened by press-fitting a pipe expanding mandrel having a slightly larger diameter. Further, the refrigerant tubes are joined by brazing or the like by using individual parts that have been bent to 180 degrees in another process, and straight tubes and 180 degree bent tubes are alternately joined to form a heat exchanger. . Fins are provided with slits as needed to increase heat exchange performance.

【0003】また、冷媒管を蛇行曲げし、かつ繋ぎ部が
ない構造のクロスフィン型熱交換器としては、特開平9
−96496号公報に記載のように、冷媒管を一筆書き
で蛇行状に加工した後に、フィンの切り欠き内に冷媒管
を押し込むカチ込む方式のものがあった。さらに、従来
より冷蔵庫用の熱交換器とくに凝縮器として一般的に使
用されているものとして、図10に示すように帯状フィ
ンF’が螺旋巻きされた冷媒管P’を平面(2次元)状
もしくは立体(3次元)状に蛇行曲げした螺旋フィン形
の熱交換器があった。
Further, as a cross fin type heat exchanger having a structure in which a refrigerant pipe is meandered and has no connecting portion, there is disclosed in Japanese Patent Laid-Open No. Hei 9 (1998)
As described in Japanese Patent Laid-Open No. 96496, there is a method in which a refrigerant pipe is processed into a meandering shape with a single stroke and then the refrigerant pipe is pushed into the notches of the fins. Further, as generally used as a heat exchanger for refrigerators, particularly as a condenser, a refrigerant pipe P ′ spirally wound with a band-shaped fin F ′ as shown in FIG. 10 has a planar (two-dimensional) shape. Alternatively, there was a spiral fin-shaped heat exchanger that was meanderingly bent into a three-dimensional shape.

【0004】[0004]

【発明が解決しようとする課題】上記従来技術の内、一
定間隔で平行に配列された複数の冷媒管と、その冷媒管
に垂直な方向に一定間隔で並べられた複数枚のフィンで
構成されていたクロスフィン型熱交換器の場合、直管と
180度曲げ管とを交互に接合して熱交換器を構成して
いるため、製品の気密性、冷媒漏れに対する信頼性を上
げようとしても、接合部の数の乗数分だけ信頼性が下が
るという問題があった。例えば、可燃性の冷媒を熱交換
に使用する際、その安全対策上、冷媒漏れの少ない構造
つまりは接合個所の少ない熱交換器構造が有効となり、
従来の構造では十分に信頼性が得られないという問題が
あった。
Of the above-mentioned prior art, it is composed of a plurality of refrigerant pipes arranged in parallel at regular intervals and a plurality of fins arranged at regular intervals in a direction perpendicular to the refrigerant pipes. In the case of the cross-fin type heat exchanger, the straight tubes and the 180-degree bent tubes are alternately joined to form the heat exchanger, so even if it is attempted to improve the airtightness of the product and the reliability against refrigerant leakage. However, there is a problem that the reliability is reduced by a multiplier of the number of joints. For example, when using a flammable refrigerant for heat exchange, in terms of safety measures, a structure with less refrigerant leakage, that is, a heat exchanger structure with fewer joints becomes effective,
The conventional structure has a problem that sufficient reliability cannot be obtained.

【0005】また、冷媒管の接合箇所をなくした、例え
ば冷媒管を一筆書きで蛇行状に加工した後に、フィンの
切り欠き部に冷媒管をカチ込む構造の熱交換器の場合、
冷媒管とフィンが全周で密着する構造とはならず、また
拡管方式に比べ冷媒管とフィンの緊縛力も劣ること、ま
た冷媒管挿入部のフィンを切り欠くことによるフィン伝
熱面積の減少から熱交換性能は拡管構造の熱交換器に比
べ劣るという問題があった。
Further, in the case of a heat exchanger having a structure in which the joint portion of the refrigerant pipe is eliminated, for example, the refrigerant pipe is processed into a meandering shape with a single stroke, and then the notch portion of the fin is clicked,
The structure in which the refrigerant pipe and the fin are not in close contact with each other on the entire circumference, the binding force between the refrigerant pipe and the fin is inferior to that of the expansion method, and the fin heat transfer area is reduced by notching the fin in the refrigerant pipe insertion part. There was a problem that the heat exchange performance was inferior to that of the heat exchanger having the tube expansion structure.

【0006】さらに、螺旋フィン形熱交換器の場合、元
々直線状の冷媒管に帯状フィンを螺旋状に巻付け、その
後蛇行状に曲げることから熱交換器の設置スペースに任
意の形状にて熱交換器を形作れるという優位点を有して
いる。しかしながら、前記螺旋フィン形の熱交換器にお
いてもフィンと冷媒管の締結形態が拡管方式ではないこ
とによる冷媒管とフィンの緊縛力が小さいこと、また円
形フィンにより隣合うフィン同士にデッドスペースが生
まれフィン伝熱面積は大きく取れない事から熱交換性能
が拡管構造のクロスフィン型熱交換器に比べ劣るという
問題があった。
Further, in the case of a spiral fin type heat exchanger, a band-shaped fin is spirally wound around an originally linear refrigerant pipe and then bent in a meandering shape, so that the heat exchanger can be installed in an arbitrary shape in the installation space of the heat exchanger. It has the advantage of being able to form exchangers. However, even in the above-mentioned spiral fin type heat exchanger, the tight binding force between the refrigerant pipe and the fin is small due to the fact that the fin and the refrigerant pipe are not connected by the expansion method, and the circular fin creates a dead space between the adjacent fins. Since the fin heat transfer area cannot be made large, there was a problem that the heat exchange performance was inferior to that of the cross-fin type heat exchanger having the expanded structure.

【0007】これらの問題を解決するため、1枚のフィ
ンに1個の通孔を設け、その通孔中に所定の冷媒管を通
した後に拡管して十分な緊縛力を得た後に、冷媒管を曲
げ加工して任意の熱交換器形状を得る方法が考えられ
る。
In order to solve these problems, one fin is provided with one through hole, and a predetermined refrigerant pipe is passed through the through hole and then expanded to obtain a sufficient binding force. A method of bending the tube to obtain an arbitrary heat exchanger shape can be considered.

【0008】本発明の目的は、その基本的構想に基づ
き、熱交換性能を確保しつつ、継目を極力少なくして冷
媒漏れに対する信頼性を高めた熱交換器を提供すること
にある。また、本発明の第2の目的は、必要最小限のフ
ィン構造を1単位とすることにより、熱交換器の設計の
自由度を上げることにある。
An object of the present invention is to provide a heat exchanger based on the basic concept thereof, which secures heat exchange performance, minimizes joints, and improves reliability against refrigerant leakage. A second object of the present invention is to increase the degree of freedom in designing the heat exchanger by using the minimum required fin structure as one unit.

【0009】[0009]

【課題を解決するための手段】上記目的を達成するため
に、1本もしくは複数本を平行に配列した長尺の冷媒管
と、その冷媒管の垂直方向に所定の間隔で平行に並べた
複数枚のフィンからなるクロスフィン型熱交換器におい
て、独立した1枚のフィンに対して冷媒管は1本のみ接
触させた構造としたものである。この独立した1枚のフ
ィンは、伝熱面積を最大にするためには四角形が望まし
いが、伝熱性能を多少犠牲にしても生産性を上げるため
には方向性を無くして円形とすることも可能である。
In order to achieve the above object, one or a plurality of long refrigerant tubes are arranged in parallel, and a plurality of refrigerant tubes are arranged in parallel in the vertical direction of the refrigerant tubes at a predetermined interval. In a cross fin type heat exchanger composed of one fin, only one refrigerant pipe is in contact with one independent fin. This independent fin is preferably a quadrangle in order to maximize the heat transfer area, but may be made circular without any directivity in order to improve productivity even if the heat transfer performance is somewhat sacrificed. It is possible.

【0010】或いは、伝熱面積を増大させる目的、若し
くは隣同士のフィンの重なりを防止する目的として、そ
の独立した1枚のフィンの1個所以上を折り返した構造
としたものである。逆に、特定の箇所だけ伝熱面積を他
の箇所よりも増大させたい場合、平行に配列した長尺の
冷媒管の間隔よりも広い幅方向のフィン構造とすること
により、隣同士の冷媒管に接合したフィンが所定の長さ
だけお互いに重なり合う構造とすることも可能である。
或いは、通風抵抗を低減させる目的で、所定の熱交換領
域で隣の冷媒管に接合したフィン同士の間に所定の間隔
を設けたものである。
Alternatively, in order to increase the heat transfer area or to prevent the adjacent fins from overlapping with each other, one or more of the independent fins are folded back. On the other hand, if you want to increase the heat transfer area only at a specific location compared to other locations, use a fin structure in the width direction that is wider than the interval between long refrigerant tubes arranged in parallel, so that adjacent refrigerant tubes It is also possible to adopt a structure in which the fins joined to each other overlap each other for a predetermined length.
Alternatively, for the purpose of reducing ventilation resistance, a predetermined gap is provided between fins joined to adjacent refrigerant tubes in a predetermined heat exchange area.

【0011】また、所定平面の熱交換領域を確保する目
的で、元々直線状の1本の冷媒管を所定箇所で任意回数
だけ1平面内で曲げ加工した構造としたものである。こ
の基本構造により、任意箇所での曲げ加工が可能となる
ため、平行に配列した長尺の冷媒管の長さを任意に設定
でき、かつそれぞれの冷媒管の長さに応じた数量だけフ
ィンを接合した熱交換器構造としたものである。この構
造において、生産性の向上を目的に、曲げ加工部を同一
の最小曲げ半径と任意の直線部の組合せによって構成さ
せたものである。また、本方式を3次元的に応用するこ
とにより、所定平面内及び所定奥行方向を持つ所定空間
の熱交換領域を確保する構造としたものである。さら
に、フィン同士の間隔を任意とした構造として設計の自
由度を向上させたものである。
Further, in order to secure a heat exchange area on a predetermined plane, an originally linear refrigerant pipe is bent at a predetermined position an arbitrary number of times in one plane. With this basic structure, it is possible to bend at any point, so the length of long refrigerant tubes arranged in parallel can be set arbitrarily, and the number of fins is set according to the length of each refrigerant tube. It has a joined heat exchanger structure. In this structure, for the purpose of improving the productivity, the bending portion is configured by a combination of the same minimum bending radius and an arbitrary straight portion. Further, by applying the present method three-dimensionally, the structure is such that a heat exchange area of a predetermined space having a predetermined plane and a predetermined depth direction is secured. Furthermore, the degree of freedom in design is improved by providing a structure in which fins are spaced at arbitrary intervals.

【0012】[0012]

【発明の実施の形態】本発明の実施例を、以下図1〜図
9を用いて説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to FIGS.

【0013】図1は、本発明の一実施例であるクロスフ
ィン型熱交換器Hを示す斜視図である。図1(a)にお
いて、冷媒管Pは8個所の直線部Ps(一部フィンFの
影になるため図示せず)と、7個所の曲げ部Pc1〜P
c7から構成されており、交互に折り返されて同一平面
内に蛇行形状としている。その冷媒管Pの直線部Psに
は、放熱用のフィンFを一定の間隔で冷媒管Pに垂直に
並べて取り付けており、独立した1枚のフィンFに対し
て冷媒管Pは1本のみ接触していることを特徴としてい
る。
FIG. 1 is a perspective view showing a cross fin type heat exchanger H which is an embodiment of the present invention. In FIG. 1 (a), the refrigerant pipe P has eight straight portions Ps (not shown because they are partially shaded by the fins F) and seven bent portions Pc1 to Pc.
It is composed of c7 and is folded back alternately to form a meandering shape in the same plane. In the straight portion Ps of the refrigerant pipe P, fins F for heat radiation are vertically arranged side by side with the refrigerant pipe P at regular intervals, and only one refrigerant pipe P contacts one independent fin F. It is characterized by doing.

【0014】図1(b)は図1(a)に示す本発明の一
実施例のバリエーションであり、冷媒管の直線部Psに
接合したフィンFのピッチ間隔を任意に設定した構造で
ある。
FIG. 1B is a variation of the embodiment of the present invention shown in FIG. 1A, and has a structure in which the pitch interval of the fins F joined to the straight portion Ps of the refrigerant pipe is arbitrarily set.

【0015】本発明の図1の実施例において、フィンF
と冷媒管Pの接触は、冷媒管Pの径を内部圧力もしくは
機械的に広げて接触させる拡管方式、或いは溶接・ロー
付け・接着・塗装など外部要因による接合方式がある。
冷媒管P及びフィンFは、銅やアルミニウム及びそれら
の合金等、熱伝導性の高い金属が主として用いられる
が、鉄及びその合金、樹脂を用いたものでもよい。また
冷媒管PとフィンFは同種の材質でも、異種の材質でも
構わない。さらに、冷媒管Pの曲げ部PcにフィンFを
接合する構造も設計上可能である。
In the embodiment of FIG. 1 of the present invention, the fin F
As for the contact between the refrigerant pipe P and the refrigerant pipe P, there are a pipe expansion system in which the diameter of the refrigerant pipe P is expanded by internal pressure or mechanical contact, or a joining system by external factors such as welding, brazing, bonding, and painting.
The refrigerant pipes P and the fins F are mainly made of a metal having high thermal conductivity such as copper, aluminum and alloys thereof, but may be made of iron, an alloy thereof and a resin. The refrigerant pipe P and the fin F may be made of the same material or different materials. Further, a structure in which the fin F is joined to the bent portion Pc of the refrigerant pipe P can be designed.

【0016】図2は、図1に示す本発明の一実施例にお
ける別の実施形態を示す斜視図である。図2(a)にお
いて、冷媒管Pは8個所の直線部Ps(一部フィンFの
影になるため図示せず)と、7個所の曲げ部Pc1〜P
c7から構成されており、交互に折り返されて同一平面
内に蛇行形状としている。その冷媒管Pの直線部Psに
は放熱用のフィンF’を一定の間隔で冷媒管Pに垂直に
並べて取り付けており、独立した1枚のフィンFに対し
て冷媒管Pは1本のみ接触している。フィンF’は円形
であるため、四角形のフィンFを接合した熱交換器に比
べて、冷媒管PにフィンF’を装着する際の方向性がな
くなり、生産性を向上させることができる。
FIG. 2 is a perspective view showing another embodiment of the embodiment of the present invention shown in FIG. In FIG. 2A, the refrigerant pipe P has eight straight portions Ps (not shown because they partially shade the fins F) and seven bent portions Pc1 to Pc.
It is composed of c7 and is folded back alternately to form a meandering shape in the same plane. In the straight portion Ps of the refrigerant pipe P, fins F ′ for heat dissipation are vertically arranged side by side with the refrigerant pipe P at regular intervals, and only one refrigerant pipe P contacts one independent fin F. is doing. Since the fins F ′ have a circular shape, the fin F ′ has no directionality when the fins F ′ are attached to the refrigerant pipe P, and productivity can be improved as compared with a heat exchanger in which the rectangular fins F are joined.

【0017】図2(b)は、図2(a)におけるフィン
Fを六角形にした場合の実施例を示す。この場合、図1
に示す実施例における最大伝熱面積、図2(a)のおけ
る最大生産性の中間の性質を示しており、この他伝熱性
能、生産性とのバランスを考慮してフィンFはいかなる
形状でも設計可能である。またフィンFそのものに切り
込みスリットや山形の折り曲げ部を設けて、フィンFそ
のものの熱交換性能を向上させた構造にも本発明は適用
可能である。
FIG. 2B shows an embodiment in which the fin F in FIG. 2A is hexagonal. In this case,
2A shows an intermediate property between the maximum heat transfer area and the maximum productivity in FIG. 2A, and the fin F may have any shape in consideration of the balance between the heat transfer performance and the productivity. It can be designed. The present invention is also applicable to a structure in which the fin F itself is provided with a slit slit or a mountain-shaped bent portion to improve the heat exchange performance of the fin F itself.

【0018】図3及び図4は、本発明の別の実施例であ
り、図1に示す本発明の一実施例のバリエーションを示
す部分斜視図である。図3において、冷媒管Pは、冷媒
管の直線部Ps1及びPs2と、冷媒管の曲げ部Pcと
で構成されており、冷媒管の直線部Ps1、Ps2に
は、放熱用のフィンFを一定の間隔で冷媒管Pに垂直に
並べて取り付けており、独立した1枚のフィンFに対し
て冷媒管Pは1本のみ接触している構造である。フィン
Fは、冷媒管接触部Fhと2個所の折り曲げ部Ffとで
構成している。フィンFを図3に示すような構造とする
ことにより、限られた領域内におけるフィンFの伝熱面
積を増大させることができ、加えて冷媒管の直線部Ps
1に接触するフィンFと、その隣の冷媒管の直線部Ps
2に接触するフィンFとが重なり合わず、かつ万が一、
冷媒管PとフィンFとの接触が甘くなった際のフィンF
の回転を防止する効果がある。図3に示す本発明の一実
施例を連続的に並べることで、図1に示すように、蛇行
状に加工した冷媒管Pを用いた平面的な熱交換器構造と
することもできる。
FIGS. 3 and 4 are partial perspective views showing another embodiment of the present invention and showing a variation of the embodiment of the present invention shown in FIG. In FIG. 3, the refrigerant pipe P is composed of the linear portions Ps1 and Ps2 of the refrigerant pipe and the bent portion Pc of the refrigerant pipe, and the fins F for heat dissipation are fixed in the linear portions Ps1 and Ps2 of the refrigerant pipe. The refrigerant pipes P are vertically arranged side by side at intervals of, and the structure is such that only one refrigerant pipe P contacts one independent fin F. The fin F includes a refrigerant pipe contact portion Fh and two bent portions Ff. By configuring the fins F as shown in FIG. 3, the heat transfer area of the fins F in a limited area can be increased, and in addition, the linear portion Ps of the refrigerant pipe can be increased.
The fin F that comes into contact with 1 and the linear portion Ps of the refrigerant pipe adjacent to the fin F
The fins F that come into contact with 2 do not overlap, and by any chance,
The fin F when the contact between the refrigerant pipe P and the fin F becomes loose
It has the effect of preventing the rotation. By continuously arranging one embodiment of the present invention shown in FIG. 3, as shown in FIG. 1, it is possible to form a planar heat exchanger structure using a refrigerant pipe P processed in a meandering shape.

【0019】図4は、熱交換器の性能上、フィンFの間
隔を部分的に狭める必要がある場合における、本発明の
一実施例を示す斜視図である。4本の冷媒管の直線部P
sが平行になるように曲げ部Pc1、Pc2、Pc3を
設け、冷媒管の直線部Ps同士のピッチ間隔よりも、そ
の冷媒管の直線部Psに接合したフィンFの幅が大きく
なるようにしたものである。そのため、フィンF同士が
重なり合う部分Foができ、冷媒管Pに取り付けられた
フィンFのピッチ間隔の2倍にあたる密度で熱交換する
箇所を設けた構造としたものである。図4に示す本発明
の一実施例を連続的に並べることで、図1に示すよう
に、蛇行状に加工した冷媒管Pを用いた平面的な熱交換
器構造とすることもできる。
FIG. 4 is a perspective view showing an embodiment of the present invention when it is necessary to partially narrow the gap between the fins F in view of the performance of the heat exchanger. Straight part P of four refrigerant tubes
The bent portions Pc1, Pc2, and Pc3 are provided so that s becomes parallel, and the width of the fin F joined to the linear portion Ps of the refrigerant pipe is larger than the pitch interval between the linear portions Ps of the refrigerant pipe. It is a thing. Therefore, there is a portion Fo in which the fins F overlap each other, and a portion is provided for heat exchange at a density that is twice the pitch interval of the fins F attached to the refrigerant pipe P. By arranging one embodiment of the present invention shown in FIG. 4 continuously, a planar heat exchanger structure using a refrigerant pipe P processed in a meandering shape can be obtained as shown in FIG.

【0020】図1〜図4に示す熱交換器は、冷媒管Pを
直線部Psと曲げ部Pcとに分けて複数個製作し、冷媒
管の直線部PsにフィンFを接合した後に冷媒管の直線
部Psと曲げ部Pcを繋ぎ合わせて構成することも可能
であるが、可燃性の冷媒を用いる時等、冷媒通路の継目
をできるだけ少なくしたい場合は、最初に長尺な直管の
冷媒管Pの所定箇所に所定数だけ所定ピッチ間隔でフィ
ンFを取り付け、後に冷媒管Pの所定箇所で所定方向に
曲げ加工することで冷媒管の直線部Psと曲げ部Pcと
を形成する方法で製作することも可能である。
In the heat exchanger shown in FIGS. 1 to 4, a plurality of refrigerant pipes P are divided into a straight portion Ps and a bent portion Pc, and a plurality of refrigerant pipes P are manufactured. It is also possible to connect the straight line portion Ps and the bent portion Pc to each other, but if it is desired to minimize the number of joints in the refrigerant passage such as when using a flammable refrigerant, first, a long straight pipe refrigerant is used. By the method of forming the linear portion Ps and the bent portion Pc of the refrigerant pipe by attaching the fins F to a predetermined portion of the pipe P with a predetermined number of pitch intervals and then bending the fin P in a predetermined direction at a predetermined portion of the refrigerant pipe P. It is also possible to produce.

【0021】この場合、故フィンFの幅よりも、冷媒管
の直線部Ps同士のピッチ間隔を大きく設定して、隣同
士の冷媒管の直線部Psに接触しているフィンF同士
を、所定間隔の空隙が設けることもできる。
In this case, the pitch interval between the linear portions Ps of the refrigerant tubes is set to be larger than the width of the late fins F, and the fins F that are in contact with the linear portions Ps of the adjacent refrigerant tubes are provided with a predetermined distance. Spaces of intervals can also be provided.

【0022】図5は、本発明を立体的に構成する場合の
一実施例の斜視図を示す。図1〜図4に示平面状の熱交
換器Hを、冷媒管の直線部Psを所定箇所Bにおいて9
0度にL字形に曲げたものであり、立体的な空間におい
て熱交換を可能とし、熱交換効率を高めた構造の熱交換
器Hである。図5(a)は、冷媒管PのL字曲げ部Bに
もフィンFを連続的に接合した実施例であり、図5
(b)は冷媒管PのL字曲げ部B’にフィンFを取り付
けない場合の冷媒管P実施例である。熱交換効率は図5
(a)に示す実施例の熱交換器の方が高く、生産性は図
5(b)に示す実施例の熱交換器の方が高い。いずれの
場合も、熱交換効率と生産性のバランスを考慮して、図
5(a)と図5(b)との中間タイプの熱交換器構造と
することもできる。この冷媒管PのL時曲げ部Bは複数
個所設けてもよく、また角度は90度以外でもよい。こ
のように本発明の熱交換器Hを搭載するにあたっての製
品の搭載スペースに合わせた形状に形成することもでき
るフレキシビリティがある。
FIG. 5 shows a perspective view of an embodiment in which the present invention is three-dimensionally constructed. The flat heat exchanger H shown in FIGS. 1 to 4 has a linear portion Ps of the refrigerant pipe at a predetermined position B.
It is a heat exchanger H that is bent in an L shape at 0 degrees, enables heat exchange in a three-dimensional space, and has a structure with improved heat exchange efficiency. FIG. 5A shows an embodiment in which fins F are continuously joined to the L-shaped bent portion B of the refrigerant pipe P.
(B) is an embodiment of the refrigerant pipe P in which the fin F is not attached to the L-shaped bent portion B ′ of the refrigerant pipe P. Figure 5 shows the heat exchange efficiency
The heat exchanger of the embodiment shown in (a) is higher, and the productivity is higher in the heat exchanger of the embodiment shown in FIG. 5 (b). In any case, in consideration of the balance between heat exchange efficiency and productivity, a heat exchanger structure of an intermediate type between those shown in FIGS. 5A and 5B can be used. The L-time bent portion B of the refrigerant pipe P may be provided at a plurality of locations, and the angle may be other than 90 degrees. As described above, there is flexibility in that the heat exchanger H of the present invention can be formed into a shape that fits the mounting space of the product.

【0023】図6は本発明を立体的に構成する場合の別
の実施例を示す斜視図である。冷媒管Pは16個所の直
線部Psと、7個所の曲げ部Pc1〜Pc7、及び8個
所のL時曲げ部Bで構成している。16個所の直線部P
sにはそれぞれ所定枚数のフィンFが所定ピッチ間隔で
接合されている。ここで冷媒管Pの各直線部は長さを任
意に設けてあり、図6に示すように、熱交換器Hの左側
にある直線部Psの長さをLa、右側の直線部Psの長
さをLbとして任意に変化をつけたものである。これに
より、例えば、長さLaの直線部Ps側に別部品を搭載
したい場合など、それを回避した形の熱交換器Hを形成
できるという特徴がある。特に、冷媒管Pの構造を継目
のない形とした場合、曲げ部PcとL字曲げ部Bの位置
を任意に設定することにより、自由な形状の熱交換器H
を提供することができる。
FIG. 6 is a perspective view showing another embodiment in which the present invention is three-dimensionally constructed. The refrigerant pipe P is composed of 16 straight portions Ps, 7 bent portions Pc1 to Pc7, and 8 bent portions B at L time. 16 straight parts P
A predetermined number of fins F are joined to s at predetermined pitch intervals. Here, each linear portion of the refrigerant pipe P is provided with an arbitrary length, and as shown in FIG. 6, the length of the linear portion Ps on the left side of the heat exchanger H is La, and the length of the linear portion Ps on the right side is La. The length is arbitrarily set as Lb. Thereby, for example, when another component is to be mounted on the straight portion Ps side of the length La, it is possible to form the heat exchanger H in a shape avoiding it. In particular, when the structure of the refrigerant pipe P is a seamless shape, by freely setting the positions of the bent portion Pc and the L-shaped bent portion B, the heat exchanger H having a free shape can be obtained.
Can be provided.

【0024】図7は、本発明の熱交換器において、冷媒
管Pの曲げ部Pcをフレキシブルに設定可能にした場合
の構造を示す説明図である。図7(a)は、フィンFを
接合した冷媒管の直線部Ps同士のピッチ間隔Paが、
冷媒管の曲げ部Pcの曲げ半径Raの2倍に等しい場合
の実施例を示す。また図7(b)は、フィンFを接合し
た冷媒管の直線部Ps同士のピッチ間隔Pbが、冷媒管
の曲げ部Pcの曲げ半径Rbの2倍より微小直線部Sb
だけ大きい場合の実施例を示す。図7(a)の実施例に
示すように、曲げ半径Raと、冷媒管の直線部Ps同士
のピッチ間隔Paとした場合、冷媒管の直線部Ps同士
のピッチ間隔Paが変化する度に、曲げ半径Raも変化
することになり、設計変更がある度に曲げ半径Raを形
成する曲げ型を交換しなければならず、設備費の負担が
大きいものとなっていた。一方、図7(b)の実施例に
示すように、曲げ半径Rbを固定して、冷媒管の直線部
Ps同士のピッチ間隔Pbが変化する際に微小直線部S
bの間隔だけ制御する構造とすることで、曲げ型は設計
段階で考え得る最小の曲げ半径Rbのものを用意するだ
けでよく、設備費低減に効果があるものとなる。なお、
微小直線部Sbは必ずしも直線である必要はなく、屈曲
させた構造でも同様の効果を得ることは可能である。ま
た、本発明のこの構造は冷媒管の曲げ部Pcだけでな
く、冷媒管のL字曲げ部Bにも適用可能である。
FIG. 7 is an explanatory view showing the structure of the heat exchanger of the present invention in which the bent portion Pc of the refrigerant pipe P can be flexibly set. FIG. 7A shows that the pitch interval Pa between the straight line portions Ps of the refrigerant pipe to which the fins F are joined is
An example is shown in which the bending radius Ra of the bent portion Pc of the refrigerant pipe is equal to twice the bending radius Ra. Further, in FIG. 7 (b), the pitch interval Pb between the straight portions Ps of the refrigerant pipe to which the fins F are joined is smaller than twice the bending radius Rb of the bent portion Pc of the refrigerant pipe.
An example in the case of only large is shown. As shown in the embodiment of FIG. 7A, when the bending radius Ra and the pitch interval Pa between the linear portions Ps of the refrigerant pipe are set, each time the pitch interval Pa between the linear portions Ps of the refrigerant tube changes, The bending radius Ra also changes, and the bending die forming the bending radius Ra must be replaced every time there is a design change, resulting in a large burden of equipment costs. On the other hand, as shown in the embodiment of FIG. 7B, when the bending radius Rb is fixed and the pitch interval Pb between the linear portions Ps of the refrigerant pipe changes, the minute linear portion S
By adopting a structure in which only the distance b is controlled, it is sufficient to prepare a bending die having a minimum bending radius Rb that can be considered in the design stage, which is effective in reducing the equipment cost. In addition,
The minute straight line portion Sb does not necessarily have to be a straight line, and the same effect can be obtained with a bent structure. Further, this structure of the present invention is applicable not only to the bent portion Pc of the refrigerant pipe but also to the L-shaped bent portion B of the refrigerant pipe.

【0025】図8は、本発明を立体的に構成する場合の
第3の実施例を示す斜視図である。図1に示した本発明
の実施例は同一平面内に冷媒管Pを成形して、平面的
(2次元的)にフィンFを配置した構造の熱交換器Hで
あるのに対して、図8に示す本発明の別実施例の熱交換
器Hは、冷媒管の直線部Ps、及び同じ平面内に曲げ加
工した曲げ部Pc1〜Pc4、並びに奥行方向に曲げ加
工した曲げ部Pc’(他の奥行方向に曲げ加工した曲げ
部は図示せず)によって構成され、立体(3次元)形状
の熱交換器構造としたものである。この実施例において
も、冷媒管Pを継目の無い構造で製作でき、冷媒管の直
線部Psの長さ、曲げ部Pc及びPc’のピッチ間隔、
並びにフィンFのピッチ間隔はこれまで示した実施例と
同様にして任意に設計製作可能である。
FIG. 8 is a perspective view showing a third embodiment when the present invention is three-dimensionally constructed. The embodiment of the present invention shown in FIG. 1 is a heat exchanger H having a structure in which a refrigerant pipe P is formed in the same plane and fins F are arranged two-dimensionally (two-dimensionally). A heat exchanger H according to another embodiment of the present invention shown in FIG. 8 includes a straight portion Ps of the refrigerant pipe, bent portions Pc1 to Pc4 bent in the same plane, and a bent portion Pc ′ (others) bent in the depth direction. The bent portion bent in the depth direction is formed by a not-shown), and has a three-dimensional (three-dimensional) shape heat exchanger structure. Also in this embodiment, the refrigerant pipe P can be manufactured with a seamless structure, the length of the straight portion Ps of the refrigerant pipe, the pitch interval between the bent portions Pc and Pc ′,
Also, the pitch interval of the fins F can be arbitrarily designed and manufactured in the same manner as in the above-described embodiments.

【0026】図9は本発明の熱交換器Hを搭載した冷蔵
庫の部分斜視図である。本図は冷蔵庫を背面から見た下
部を示したもので、側板M1、M2、底板M3、蒸発皿
Eによって囲まれた空間に、冷媒の凝縮サイクル系を搭
載した構造を示すものである。本発明である、冷媒管P
とフィンFで構成される熱交換器HはコンプレッサCで
圧縮された冷媒を冷媒管Pに通して、この熱交換器Hに
おいて放熱するものである。熱交換器Hにおいて放熱さ
れた熱量はファンVによって起こされる空気の強制対流
によって外界に流される。
FIG. 9 is a partial perspective view of a refrigerator equipped with the heat exchanger H of the present invention. This figure shows the lower part of the refrigerator when viewed from the back side, and shows a structure in which a refrigerant condensing cycle system is mounted in a space surrounded by side plates M1, M2, a bottom plate M3, and an evaporating dish E. The refrigerant pipe P according to the present invention
The heat exchanger H constituted by the fins F is configured to pass the refrigerant compressed by the compressor C through the refrigerant pipe P and radiate the heat in the heat exchanger H. The amount of heat radiated in the heat exchanger H is flown to the outside by forced convection of air caused by the fan V.

【0027】本発明の熱交換器は、図9に示す冷蔵庫背
面の凝縮サイクル以外にも、冷蔵庫内部の蒸発サイク
ル、空調機の熱交換器、冷凍機や除湿機の熱交換器にも
適用可能である。
The heat exchanger of the present invention can be applied not only to the condensation cycle on the back of the refrigerator shown in FIG. 9 but also to the evaporation cycle inside the refrigerator, the heat exchanger for air conditioners, the heat exchanger for refrigerators and dehumidifiers. Is.

【0028】以上説明した実施形態により、従来タイプ
の熱交換器と熱交換性能や伝熱性能を維持しつつ、継目
を極力少なくして冷媒漏れに対する信頼性を高めた熱交
換器を提供できるものである。また、必要最小限のフィ
ン構造を1単位とすることにより、熱交換器の設計製作
の自由度を上げることができる。
According to the above-described embodiment, it is possible to provide a heat exchanger which maintains the heat exchange performance and the heat transfer performance as compared with the conventional type heat exchanger while minimizing the joints and improving the reliability against refrigerant leakage. Is. In addition, by setting the minimum required fin structure as one unit, the degree of freedom in designing and manufacturing the heat exchanger can be increased.

【0029】[0029]

【発明の効果】本発明により、従来の熱交換器以上の熱
交換性能を維持しつつ、継目を極力少なくして気密信頼
性を高めた熱交換器を提供できる効果がある。これによ
り、炭化水素系の可燃性の冷媒を用いた場合でも、製品
信頼性を向上させることができる効果がある。また、必
要最小限のフィン構造を1単位とし、最小曲げ半径と任
意の直線部を組合せ、3次元的に曲げ加工することによ
り、任意形状の熱交換器が製作可能となり、設計自由度
を高い熱交換器を提供できる効果がある。
EFFECTS OF THE INVENTION The present invention has the effect of providing a heat exchanger having a heat-sealing performance higher than that of a conventional heat exchanger, the number of joints being minimized, and the hermetic reliability being improved. As a result, the product reliability can be improved even when a hydrocarbon-based flammable refrigerant is used. In addition, the minimum required fin structure is set as one unit, and the minimum bending radius and an arbitrary straight line portion are combined and three-dimensionally bent, so that a heat exchanger of any shape can be manufactured, and the degree of freedom in design is high. There is an effect that a heat exchanger can be provided.

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

【図1】本発明の一実施例であるクロスフィン型熱交換
器を示す斜視図。
FIG. 1 is a perspective view showing a cross fin type heat exchanger according to an embodiment of the present invention.

【図2】本発明の一実施例における別の実施形態を示す
斜視図。
FIG. 2 is a perspective view showing another embodiment in one example of the present invention.

【図3】本発明の一実施例のバリエーションを示す部分
斜視図。
FIG. 3 is a partial perspective view showing a variation of the embodiment of the present invention.

【図4】本発明の一実施例のバリエーションを示す部分
斜視図。
FIG. 4 is a partial perspective view showing a variation of the embodiment of the present invention.

【図5】本発明を立体的に構成する場合の一実施例の斜
視図。
FIG. 5 is a perspective view of an embodiment when the present invention is three-dimensionally configured.

【図6】本発明を立体的に構成する場合の別の実施例を
示す斜視図。
FIG. 6 is a perspective view showing another embodiment when the present invention is three-dimensionally configured.

【図7】本発明の熱交換器において冷媒管の曲げ部をフ
レキシブルに設定可能にした場合の構造を示す説明図。
FIG. 7 is an explanatory view showing the structure of the heat exchanger of the present invention when the bent portion of the refrigerant pipe can be flexibly set.

【図8】本発明を立体的に構成する場合の第3の実施例
を示す斜視図。
FIG. 8 is a perspective view showing a third embodiment when the present invention is three-dimensionally configured.

【図9】本発明の熱交換器を搭載した冷蔵庫の部分斜視
図。
FIG. 9 is a partial perspective view of a refrigerator equipped with the heat exchanger of the present invention.

【図10】従来技術である、帯状フィンが螺旋巻きされ
た冷媒管を示す図。
FIG. 10 is a view showing a refrigerant pipe in which band-shaped fins are spirally wound, which is a conventional technique.

【符号の説明】[Explanation of symbols]

F…フィン、P…冷媒管、H…熱交換器、Pc…冷媒管
の曲げ部、Ps…冷媒管の直線部、B…熱交換器のL字
曲げ部。
F ... Fin, P ... Refrigerant tube, H ... Heat exchanger, Pc ... Bent portion of refrigerant tube, Ps ... Straight portion of refrigerant tube, B ... L-shaped bent portion of heat exchanger.

フロントページの続き (72)発明者 久保田 剛 栃木県下都賀郡大平町大字富田800番地 株式会社日立製作所冷熱事業部内 (72)発明者 網本 俊之 東京都千代田区神田駿河台四丁目6番地 株式会社日立製作所内Continued front page    (72) Inventor Tsuyoshi Kubota             800 Tomita, Ohira-cho, Shimotsuga-gun, Tochigi             Hitachi Co., Ltd., Cooling & Heat Division (72) Inventor Toshiyuki Amimoto             4-6 Kanda Surugadai, Chiyoda-ku, Tokyo             Within Hitachi, Ltd.

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】1本もしくは複数本を平行に配列した長尺
の冷媒管と、その冷媒管と垂直に所定の間隔で平行に並
べた複数枚のフィンからなるクロスフィン型熱交換器に
おいて、独立した1枚のフィンに対して冷媒管は1本の
み接触していることを特徴とする熱交換器。
1. A cross fin type heat exchanger comprising a long refrigerant pipe in which one or a plurality of pipes are arranged in parallel, and a plurality of fins arranged in parallel with the refrigerant pipe in parallel at a predetermined interval, A heat exchanger characterized in that only one refrigerant pipe is in contact with one independent fin.
【請求項2】1本もしくは複数本を平行に配列した長尺
の冷媒管と、その冷媒管の垂直方向に所定の間隔で平行
に並べた複数枚のフィンからなるクロスフィン型熱交換
器において、独立した1枚のフィンが方形若しくは円形
であることを特徴とする請求項1に記載の熱交換器。
2. A cross fin type heat exchanger comprising a long refrigerant pipe in which one or a plurality of pipes are arranged in parallel and a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipe. The heat exchanger according to claim 1, wherein the single independent fin has a rectangular shape or a circular shape.
【請求項3】1本もしくは複数本を平行に配列した長尺
の冷媒管と、その冷媒管の垂直方向に所定の間隔で平行
に並べた複数枚のフィンからなるクロスフィン型熱交換
器において、独立した1枚のフィンの1個所以上を折り
返した構造とすることを特徴とする請求項1に記載の熱
交換器。
3. A cross fin heat exchanger comprising one or more long refrigerant pipes arranged in parallel and a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipes. The heat exchanger according to claim 1, wherein one or more independent fins are folded back at one or more locations.
【請求項4】複数本を平行に配列した長尺の冷媒管と、
その冷媒管の垂直方向に所定の間隔で平行に並べた複数
枚のフィンからなるクロスフィン型熱交換器において、
平行に配列した長尺の冷媒管の間隔よりも広い幅方向の
フィン構造により、隣同士の冷媒管に接合したフィンが
所定の長さだけお互いに重なり合う構造としたことを特
徴とする熱交換器。
4. A long refrigerant pipe in which a plurality of pipes are arranged in parallel,
In a cross fin type heat exchanger consisting of a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipe,
A heat exchanger characterized by a fin structure in the width direction wider than the interval between long refrigerant tubes arranged in parallel, so that fins joined to adjacent refrigerant tubes overlap each other for a predetermined length. .
【請求項5】複数本を平行に配列した長尺の冷媒管と、
その冷媒管の垂直方向に所定の間隔で平行に並べた複数
枚のフィンからなるクロスフィン型熱交換器において、
元々直線状の1本の冷媒管を所定箇所で任意回数だけ1
平面内で曲げ加工して、所定平面の熱交換領域を確保し
た構造としたことを特徴とする請求項1に記載の熱交換
器。
5. A long refrigerant pipe in which a plurality of pipes are arranged in parallel,
In a cross fin type heat exchanger consisting of a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipe,
Originally one linear refrigerant pipe at a predetermined location 1 times
The heat exchanger according to claim 1, wherein the heat exchanger has a structure in which a heat exchange region of a predetermined plane is secured by bending in a plane.
【請求項6】複数本を平行に配列した長尺の冷媒管と、
その冷媒管の垂直方向に所定の間隔で平行に並べた複数
枚のフィンからなるクロスフィン型熱交換器において、
所定の熱交換領域で隣の冷媒管に接合したフィン同士の
間に所定の間隔を設けた構造としたことを特徴とする請
求項1に記載の熱交換器。
6. A long refrigerant pipe in which a plurality of pipes are arranged in parallel,
In a cross fin type heat exchanger consisting of a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipe,
The heat exchanger according to claim 1, wherein the heat exchanger has a structure in which a predetermined gap is provided between fins joined to adjacent refrigerant pipes in a predetermined heat exchange region.
【請求項7】複数本を平行に配列した長尺の冷媒管と、
その冷媒管の垂直方向に所定の間隔で平行に並べた複数
枚のフィンからなるクロスフィン型熱交換器において、
平行に配列した長尺の冷媒管の長さが任意であり、かつ
それぞれの冷媒管の長さに応じた数量だけフィンを接合
した構造としたことを特徴とする請求項1に記載の熱交
換器。
7. A long refrigerant pipe in which a plurality of pipes are arranged in parallel,
In a cross fin type heat exchanger consisting of a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipe,
The heat exchange according to claim 1, characterized in that the lengths of the long refrigerant tubes arranged in parallel are arbitrary, and the fins are joined in an amount corresponding to the length of each refrigerant tube. vessel.
【請求項8】複数本を平行に配列した長尺の冷媒管と、
その冷媒管の垂直方向に所定の間隔で平行に並べた複数
枚のフィンからなるクロスフィン型熱交換器において、
元々直線状の1本の冷媒管を所定箇所で任意回数だけ1
平面内で曲げ加工して、所定平面の熱交換領域を確保す
る際に、同一の最小曲げ半径と任意の直線部の組合せに
よって冷媒管同士の間隔を任意の構造としたことを特徴
とする請求項5に記載の熱交換器。
8. A long refrigerant pipe in which a plurality of pipes are arranged in parallel,
In a cross fin type heat exchanger consisting of a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipe,
Originally one linear refrigerant pipe at a predetermined location 1 times
When bending in a plane to secure a heat exchange area of a predetermined plane, the interval between the refrigerant pipes is set to an arbitrary structure by a combination of the same minimum bending radius and an arbitrary straight line portion. Item 5. The heat exchanger according to item 5.
【請求項9】複数本を平行に配列した長尺の冷媒管と、
その冷媒管の垂直方向に所定の間隔で平行に並べた複数
枚のフィンからなるクロスフィン型熱交換器において、
元々直線状の1本の冷媒管を所定箇所で任意回数だけ任
意方向に曲げ加工して、所定平面内及び所定奥行方向を
持つ所定空間の熱交換領域を確保する構造としたことを
特徴とする請求項1に記載の熱交換器。
9. A long refrigerant pipe in which a plurality of pipes are arranged in parallel,
In a cross fin type heat exchanger consisting of a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipe,
The structure is characterized in that a single originally linear refrigerant pipe is bent at an arbitrary number of times in an arbitrary direction at a predetermined location to secure a heat exchange region of a predetermined space having a predetermined plane and a predetermined depth direction. The heat exchanger according to claim 1.
【請求項10】1本もしくは複数本を平行に配列した長
尺の冷媒管と、その冷媒管の垂直方向に所定の間隔で平
行に並べた複数枚のフィンからなるクロスフィン型熱交
換器において、フィン同士の間隔を任意としたことを特
徴とする請求項1〜9に記載の熱交換器。
10. A cross fin type heat exchanger comprising one or a plurality of long refrigerant pipes arranged in parallel and a plurality of fins arranged in parallel at a predetermined interval in the vertical direction of the refrigerant pipes. The heat exchanger according to any one of claims 1 to 9, wherein the fins have an arbitrary interval.
【請求項11】請求項1〜10に記載の熱交換器を凝縮
器並びに蒸発器として搭載したことを特徴とする冷蔵庫
並びに空調機、およびその他の冷凍応用製品。
11. A refrigerator, an air conditioner, and other refrigeration application products, which are equipped with the heat exchanger according to any one of claims 1 to 10 as a condenser and an evaporator.
JP2002075386A 2002-03-19 2002-03-19 Heat exchanger Withdrawn JP2003269880A (en)

Priority Applications (1)

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Publications (1)

Publication Number Publication Date
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Family

ID=29204474

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005331233A (en) * 2004-04-29 2005-12-02 Hewlett-Packard Development Co Lp Multipath heat exchanger having gap between fins of adjacent pipe portions
JP2020046173A (en) * 2019-12-24 2020-03-26 三菱電機株式会社 Outdoor unit and refrigeration cycle device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005331233A (en) * 2004-04-29 2005-12-02 Hewlett-Packard Development Co Lp Multipath heat exchanger having gap between fins of adjacent pipe portions
JP2020046173A (en) * 2019-12-24 2020-03-26 三菱電機株式会社 Outdoor unit and refrigeration cycle device

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