JP2000234883A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JP2000234883A JP2000234883A JP3827399A JP3827399A JP2000234883A JP 2000234883 A JP2000234883 A JP 2000234883A JP 3827399 A JP3827399 A JP 3827399A JP 3827399 A JP3827399 A JP 3827399A JP 2000234883 A JP2000234883 A JP 2000234883A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- flat tube
- cover material
- plate fin
- flat
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000005219 brazing Methods 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims description 43
- 239000000956 alloy Substances 0.000 claims description 6
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 229910045601 alloy Inorganic materials 0.000 claims 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- 230000007797 corrosion Effects 0.000 abstract description 6
- 238000005260 corrosion Methods 0.000 abstract description 6
- 101100008046 Caenorhabditis elegans cut-2 gene Proteins 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 230000005494 condensation Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 229910000838 Al alloy Inorganic materials 0.000 description 3
- 238000005304 joining Methods 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- 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
- F28F1/24—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 extending transversely
- F28F1/32—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 extending transversely the means having portions engaging further tubular elements
-
- 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
- F28D1/053—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 straight
- F28D1/0535—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 straight the conduits having a non-circular cross-section
- F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
- F28D1/05391—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F17/00—Removing ice or water from heat-exchange apparatus
- F28F17/005—Means for draining condensates from heat exchangers, e.g. from evaporators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2215/00—Fins
- F28F2215/12—Fins with U-shaped slots for laterally inserting conduits
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]
【発明の属する技術分野】この発明は、カーエアコン用
コンデンサやエバポレータを始めとする各種の冷暖房
機、冷凍機等に用いられる熱交換器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger used for various types of air conditioners, such as condensers for car air conditioners and evaporators, and refrigerators.
【0002】[0002]
【従来の技術】カーエアコン用のコンデンサやエバポレ
ータ等に使用される熱交換器として、図5に示すよう
に、所要間隔を置いて対峙した一対の丸パイプからなる
ヘッダー(11A)(11B)間に、各々両端を両ヘッダー
(11A)(11B)に連通接続した多数本の偏平チューブ
(12)…が相互間にコルゲートフィン(13)を介して平
行配置してコア部(14)を構成し、両ヘッダー(11A)
(11B)内の仕切り(15)により、導入口(16)から流
入する熱交換媒体がチューブ(12)…を通してコア部
(14)を蛇行状に流れて導出口(17)に至るように設定
されたものが汎用されている。また、上記一対のヘッダ
ーを用いず、一本の偏平チューブを一定長さで折り返す
形に曲成した蛇行状のサーペインタインチューブを用
い、その多段に配置した直線部間にコルゲートフィンを
介在させて同様のコア部を構成したものもある。2. Description of the Related Art As a heat exchanger used for a condenser or an evaporator for a car air conditioner, as shown in FIG. 5, a header (11A) (11B) comprising a pair of round pipes facing each other at a required interval. A number of flat tubes (12) each having both ends connected to both headers (11A) (11B) are arranged in parallel with each other via corrugated fins (13) to form a core portion (14). , Both headers (11A)
The partition (15) in the (11B) is set so that the heat exchange medium flowing from the inlet (16) flows in a meandering manner through the core (14) through the tubes (12) to the outlet (17). What has been done is widely used. In addition, without using the pair of headers, a serpentine tubing tube bent into a shape in which one flat tube is folded at a fixed length is used, and corrugated fins are interposed between linear portions arranged in multiple stages. In some cases, a similar core portion is formed.
【0003】ところで、これら熱交換器のコア部に使用
されるコルゲートフィンは、空気との接触面積を大きく
して熱交換効率を高めるものであるが、蛇行状に折り返
した形態であるために熱交換に伴って生じる結露水の排
水性が悪く、熱交換器が設置状態で図6(イ)の如く偏
平チューブ(12)…を水平とするタイプと、同図(ロ)
の如く偏平チューブ(12)…を垂直とするタイプのいず
れにおいても、図示するようにフィン(13)の狭間に水
滴(d)が溜まり易く、これによって熱交換効率が低下
したり、偏平チューブ(12)…の腐食劣化が促進される
という難点があった。[0003] The corrugated fins used in the cores of these heat exchangers increase the heat exchange efficiency by increasing the contact area with air, but have a meandering form so as to increase the heat exchange efficiency. The type in which the flat tubes (12) ... are horizontal as shown in Fig. 6 (a) with the heat exchanger installed due to poor drainage of the condensed water generated by the replacement, and Fig. 6 (b)
In any of the types in which the flat tubes (12)... Are vertical, water droplets (d) tend to accumulate between the fins (13) as shown in FIG. 12) There was a drawback that corrosion deterioration of ... was accelerated.
【0004】これに対し、図4(イ)(ロ)に示すよう
に、垂直状態で左右方向に所定間隔置きに配列した多数
枚の平板状のプレートフィン(1)…と、これらプレー
トフィン(1)…の一側端より幅方向に凹入する切欠部
(2)…に水平状態で嵌入して上下多段に配置した偏平
チューブ(3)…とでコア部(10)を構成した熱交換器
(例えば特開平6−50688号公報)では、垂直なプ
レートフィン(1)…の両側部が偏平チューブ(3)…
よりも前後に張出した形になるため、この張出した両側
部を伝って水滴が落下し易く、結露水の排水性に優れる
という利点がある。なお、図4(イ)におけるコア部
(10)の中間部分ではプレートフィン(1)及び偏平チ
ューブ(3)の図示を省略してある。また、図4(イ)
中の(4A)(4B)は垂直に配置した丸パイプ状のヘ
ッダー、(5A)は熱交換媒体の導入口、(5B)は同
導出口、図4(ロ)中の(1a)はプレートフィン
(1)のルーバー加工による凹凸条である。On the other hand, as shown in FIGS. 4 (a) and 4 (b), a plurality of flat plate fins (1)... 1) A heat exchange in which a core portion (10) is constituted by a flat tube (3) which is horizontally fitted into a notch portion (2) which is recessed in a width direction from one side end and which is arranged in upper and lower tiers. (For example, JP-A-6-50688), both sides of a vertical plate fin (1) are flat tubes (3).
Since it has a shape that protrudes forward and backward, water droplets easily fall along the protruding both sides, and there is an advantage that drainage of dew condensation water is excellent. The plate fin (1) and the flat tube (3) are not shown in the middle part of the core (10) in FIG. In addition, FIG.
(4A) and (4B) are vertically arranged round pipe headers, (5A) is an inlet for the heat exchange medium, (5B) is the outlet, and (1a) is a plate in FIG. The fins (1) are ridges formed by louver processing.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、上記の
ようなプレートフィン(1)…と偏平チューブ(3)…
とでコア部(10)を構成した熱交換器においても、偏平
チューブ(3)…の表面には常時ある程度の結露水が付
着した状態となることが避けられず、これによって偏平
チューブ(3)…の腐食劣化が進むことになる。また、
上記のコア部(10)の構成では、プレートフィン(1)
…と偏平チューブ(3)…とを炉中ロウ付けによって一
体に接合する必要があるが、この接合のためにプレート
フィン(1)…としてブレジングシートを用いた場合、
炉中ロウ付け時のロウ材の溶融に伴う肉厚減少によって
フィン強度が低下する上、フィンの空気に対する接触性
を高める上で一般的に施されるルーバー加工において、
使用する金型が磨耗損壊し易くなるという難点もあっ
た。However, the above plate fins (1) and flat tubes (3) are used.
Also in the heat exchanger having the core portion (10), it is inevitable that a certain amount of dew water is always attached to the surface of the flat tubes (3). Corrosion degradation of... Proceeds. Also,
In the configuration of the core part (10), the plate fin (1)
And the flat tube (3) must be integrally joined by brazing in a furnace. When a brazing sheet is used as the plate fin (1) for this joining,
In the louver processing which is generally performed in order to increase the fin strength due to the decrease in the fin strength due to the reduction in wall thickness due to the melting of the brazing material at the time of furnace brazing,
There was also a drawback that the mold used was liable to wear and break.
【0006】この発明は、上述の事情に鑑みて、垂直状
態で左右方向に配列したプレートフィンと、水平状態で
上下多段に配置した偏平チューブとでコア部を構成する
熱交換器として、結露水による偏平チューブの耐蝕性を
大きく向上でき、しかもプレートフィンと偏平チューブ
とを炉中ロウ付けにて確実に接合一体化でき、またプレ
ートフィンの強度を確保できると共にそのルーバー加工
に支障を生じないものを提供することを目的としてい
る。SUMMARY OF THE INVENTION In view of the above-mentioned circumstances, the present invention provides a heat exchanger having a core portion composed of plate fins arranged vertically in the left-right direction and flat tubes arranged in multiple stages in the horizontal state. The plate fin and the flat tube can be reliably joined and integrated by brazing in the furnace, and the strength of the plate fin can be secured and there is no hindrance to its louver processing. It is intended to provide.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に、この発明の請求項1に係る熱交換器は、垂直状態で
左右方向に所定間隔置きに配列した多数枚のプレートフ
ィンと、これらプレートフィンの一側端より幅方向に凹
入する切欠部に水平状態で嵌入して上下多段に配置した
偏平チューブとでコア部が構成され、このコア部の偏平
チューブ内を流れる熱交換媒体と外部の空気との間で熱
交換を行う熱交換器において、前記偏平チューブが、そ
の一側端から上下面主要部を覆う側面視略U字形のブレ
ジングシート製のカバー材を介して、前記プレートフィ
ンの切欠部に嵌入されて当該プレートフィンと接合一体
化してなることを特徴としている。In order to achieve the above object, a heat exchanger according to a first aspect of the present invention comprises a plurality of plate fins which are vertically arranged at predetermined intervals in the left-right direction. A core portion is formed by flat tubes arranged horizontally in a notch portion recessed in the width direction from one side end of the plate fin and arranged vertically in multiple stages, and a heat exchange medium flowing through the flat tubes of the core portion. In a heat exchanger that performs heat exchange with external air, the flat tube is provided with a cover material made of a brazing sheet, which is substantially U-shaped in a side view and covers a main part of the upper and lower surfaces from one end thereof. It is characterized in that it is fitted into the notch of the plate fin and joined and integrated with the plate fin.
【0008】この請求項1の構成では、偏平チューブは
その一側端から上下面主要部をカバー材にて覆われてい
るため、結露水による腐食劣化を生じにくく高い耐久性
を発揮する。そして、カバー材がブレジングシートから
なるため、炉中ロウ付けの際にカバー材のロウ材によっ
てプレートフィンと偏平チューブとが確実に接合一体化
すると共に、プレートフィンはアルミニウム合金等の通
常の材質でよいためにロウ付け時の肉厚減少による強度
低下がなく、またプレートフィンに対してルーバー加工
を支障なく施せる。According to the first aspect of the present invention, the flat tube has its upper and lower main portions covered with a cover material from one end thereof, so that the flat tube does not easily deteriorate due to dew condensation and exhibits high durability. Since the cover material is made of brazing sheet, the plate fin and the flat tube are securely bonded and integrated by the brazing material of the cover material during brazing in the furnace, and the plate fin is made of a normal material such as an aluminum alloy. Therefore, there is no reduction in strength due to a decrease in wall thickness at the time of brazing, and louver processing can be performed on the plate fins without any trouble.
【0009】請求項2の発明は、前記請求項1の熱交換
器において、前記偏平チューブ及びカバー材が共にアル
ミニウム系合金からなり、且つカバー材が偏平チューブ
の合金材料よりも電位的に卑な合金材料である構成とし
ている。この場合、炉中ロウ付けの際に偏平チューブよ
りも腐食性の高いカバー材の成分が類似材質の偏平チュ
ーブの表面に拡散し、これが犠牲防食材として機能する
から、偏平チューブ自体の耐蝕性、耐久性がより向上す
ることになる。According to a second aspect of the present invention, in the heat exchanger of the first aspect, the flat tube and the cover material are both made of an aluminum alloy, and the cover material is lower in potential than the alloy material of the flat tube. The structure is made of an alloy material. In this case, the components of the cover material, which is more corrosive than the flat tube, are diffused to the surface of the flat tube made of a similar material during brazing in the furnace, and this functions as a sacrificial anticorrosion material. The durability will be further improved.
【0010】請求項3の発明は、前記請求項1又は2の
熱交換器において、前記カバー材の外周面に、前記プレ
ートフィンの周縁を嵌合させる溝部を有してなる構成と
している。この構成では、コア部を組み立てる際、各プ
レートフィンの切欠部をカバー材の溝部に嵌合させるこ
とにより、プレートフィンを簡単に位置決めして正確に
配列させることができる上、嵌合状態でロウ付け接合さ
れるため、コア部全体の接合強度が大きく向上する。According to a third aspect of the present invention, in the heat exchanger according to the first or second aspect, a groove is provided on an outer peripheral surface of the cover member to fit a peripheral edge of the plate fin. In this configuration, when assembling the core portion, the notch portion of each plate fin is fitted into the groove of the cover material, so that the plate fins can be easily positioned and accurately arranged. Since they are attached and joined, the joining strength of the entire core portion is greatly improved.
【0011】[0011]
【発明の実施の形態】以下、この発明に係る熱交換器の
実施例について、図面を参照して具体的に説明する。図
1(イ)(ロ)は第一実施例、図2(イ)(ロ)は第二
実施例、図3(イ)〜(ハ)は第三実施例を示す。な
お、これら実施例では、既述した図4(イ)(ロ)で示
す熱交換器と共通の部分については同一符号を付してい
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the heat exchanger according to the present invention will be specifically described with reference to the drawings. FIGS. 1A and 1B show a first embodiment, FIGS. 2A and 2B show a second embodiment, and FIGS. 3A to 3C show a third embodiment. In these examples, the same reference numerals are given to the same parts as those of the heat exchangers shown in FIGS.
【0012】第一実施例を示す図1(イ)(ロ)におい
て、(1)は帯板状のプレートフィン、(3)は内部が
仕切り壁(3a)によって幅方向複数本の流路(30)に
区割された押出型材よりなる偏平チューブ、(6A)は
側面視略U字形に曲成されたブレジングシート製のカバ
ー材である。これらはいずれもアルミニウム合金製であ
るが、カバー材(6A)の合金材料はZn、Sn、In
等の元素添加によって偏平チューブの合金材料よりも電
位的に卑な材質に設定されている。In FIGS. 1 (a) and 1 (b) showing the first embodiment, (1) is a band-shaped plate fin, and (3) is a plurality of channels (3) in the width direction formed by partition walls (3a). A flat tube made of an extruded material divided into 30), and (6A) is a covering material made of a brazing sheet bent in a substantially U shape in side view. These are all made of aluminum alloy, but the alloy material of the cover material (6A) is Zn, Sn, In.
The material is set to a material which is more potential than the alloy material of the flat tube by adding elements such as.
【0013】プレートフィン(1)は、図4(イ)に示
すように、熱交換器のコア部(10)において、多数枚が
長手方向を垂直として左右方向に所定間隔置きに配列さ
れるものであり、その一側端より幅方向に凹入する切欠
部(2)…が長手方向一定間隔置きに形成されると共
に、表面にはルーバー加工によって長手方向に沿う凹凸
条(1a)…が設けられている。しかして、各切欠部
(2)は、長さが偏平チューブ(3)の幅より大きく、
且つ上下幅が偏平チューブ(3)にカバー材(6A)を
被せた状態での厚さに略一致するように設定されてい
る。As shown in FIG. 4A, a large number of plate fins (1) are arranged at predetermined intervals in the left-right direction with the longitudinal direction being vertical in the core portion (10) of the heat exchanger. Notches (2) ... which are recessed in the width direction from one side end thereof are formed at regular intervals in the longitudinal direction, and uneven surfaces (1a) ... along the longitudinal direction are provided on the surface by louver processing. Have been. Thus, each notch (2) has a length greater than the width of the flat tube (3),
In addition, the vertical width is set to substantially match the thickness of the flat tube (3) with the cover material (6A) covered.
【0014】カバー材(6A)は、U字形の曲成状態で
の幅が偏平チューブ(3)の幅よりも若干短く、且つU
字形の内側開き幅が偏平チューブ(3)の厚さと略一致
するように設定されている。The cover member (6A) has a U-shaped bent width that is slightly shorter than the width of the flat tube (3).
The opening width of the inside of the character is set so as to substantially match the thickness of the flat tube (3).
【0015】熱交換器のコア部(10)〔図4(イ)参
照〕の組立ては、所定間隔置きに配列させたプレートフ
ィン(1)…の長手方向各位置における切欠部(2)…
間にわたり、各偏平チューブ(3)を嵌合させたのち、
この嵌合部分の隙間に入り込むようにカバー材(6A)
を嵌め込むか、もしくは各偏平チューブ(3)に予めカ
バー材(6A)を被せた状態として、この両者(3)
(6A)を前記切欠部(2)…間にわたり嵌合させるこ
とにより、図1(ロ)で示す組立状態とすればよい。そ
して、図4(イ)で示すようにヘッダー(4A)(4
B)及び導出入口(5A)(5B)を含めて熱交換器全
体を組み付けた状態で、炉中ロウ付けを行うことによ
り、全体を接合一体化する。The assembling of the core portion (10) of the heat exchanger (see FIG. 4A) is performed by cutting out notches (2) at each position in the longitudinal direction of the plate fins (1) arranged at predetermined intervals.
After fitting each flat tube (3) over
Cover material (6A) so as to enter the gap of this fitting part
Or a state where each flat tube (3) is covered with a cover material (6A) in advance.
By fitting (6A) between the notches (2)..., The assembled state shown in FIG. Then, as shown in FIG. 4A, the header (4A) (4
In the state where the entire heat exchanger including B) and the outlets (5A) and (5B) is assembled, brazing is performed in a furnace to join and integrate the whole.
【0016】この炉中ロウ付けの際に、カバー材(6
A)…のロウ材が溶解することにより、プレートフィン
(1)…と偏平チューブ(3)…とがカバー材(6A)
…を介して強固に接合一体化するが、同時にカバー材
(6A)の成分が偏平チューブ(3)の表面に拡散す
る。When brazing in the furnace, the cover material (6
A) When the brazing material is dissolved, the plate fins (1) and the flat tubes (3) are covered with the cover material (6A).
..., but the components of the cover material (6A) are simultaneously diffused to the surface of the flat tube (3).
【0017】従って、得られる熱交換器においては、各
プレートフィン(1)の幅方向両側部が偏平チューブ
(3)よりも前後に張出した形態であることによって結
露水の水滴が伝い落ち易いことに加えて、偏平チューブ
(3)がその一側端から上下面主要部をカバー材(6
A)にて覆われ、しかも該偏平チューブ(3)の表面に
拡散したカバー材(6A)の成分が犠牲防食材として機
能するから、該偏平チューブ(3)は結露水による腐食
劣化を生じにくく極めて高い耐久性を発揮する。また、
プレートフィン(1)は、ロウ材を含まないためにロウ
付け時の肉厚減少がなく、充分なフィン強度を確保でき
る一方、それ自体の製作時にルーバー加工を支障なく施
せる。Accordingly, in the obtained heat exchanger, since the both sides in the width direction of each plate fin (1) project forward and backward from the flat tube (3), the water droplets of the condensed water are easily transmitted down. In addition to the above, a flat tube (3) covers a main part of the upper and lower surfaces from one side end thereof (6).
Since the component of the cover material (6A) covered with A) and diffused on the surface of the flat tube (3) functions as a sacrificial anticorrosive material, the flat tube (3) is less likely to be corroded and deteriorated by dew condensation water. Demonstrate extremely high durability. Also,
Since the plate fin (1) does not contain a brazing material, there is no decrease in wall thickness at the time of brazing, and sufficient fin strength can be secured, while louver processing can be performed without any trouble at the time of manufacturing itself.
【0018】図2(イ)(ロ)に示す第二実施例では、
プレートフィン(1)及び偏平チューブ(3)は前記第
一実施例と同様であるが、カバー材(6B)はU字形の
曲成状態での幅がプレートフィン(1)の切欠部(2)
の長さと略一致するように設定されている。しかして、
熱交換器のコア部(10)〔図4(イ)参照〕の組立て
は、所定間隔置きに配列させたプレートフィン(1)…
の長手方向各位置における切欠部(2)…間にわたり、
先にカバー材(6B)をそのU字形の曲がり側を奥側と
して嵌合させ、この嵌合したカバー材(6B)の内側に
偏平チューブ(3)を挿嵌するか、もしくは各カバー材
(6B)に偏平チューブ(3)を予め嵌め込んだ状態
で、やはりカバー材(6B)の曲がり側を奥側として前
記切欠部(2)…間にわたり嵌合させれることにより、
図2(ロ)で示す組立状態とすればよい。以降の炉中ロ
ウ付けは前記第一実施例と同様である。In the second embodiment shown in FIGS.
The plate fin (1) and the flat tube (3) are the same as in the first embodiment, but the width of the cover member (6B) in the U-shaped bent state is the notch (2) of the plate fin (1).
Is set to approximately match the length. Then
The assembling of the core part (10) of the heat exchanger (see FIG. 4A) is performed by arranging plate fins (1) at predetermined intervals.
Notch (2) at each position in the longitudinal direction of
First, the cover member (6B) is fitted with its U-shaped bent side as the back side, and a flat tube (3) is inserted inside the fitted cover member (6B), or each cover member ( 6B) with the flat tube (3) fitted in advance, with the bent side of the cover member (6B) also fitted over the notches (2)...
The assembled state shown in FIG. Subsequent brazing in the furnace is the same as in the first embodiment.
【0019】この第二実施例の熱交換器は、空気の流れ
が図2(ロ)中の矢印aで示す方向となる設置状態で使
用する。この場合、カバー材(6B)がプレートフィン
(1)の切欠部(2)の全体にわたる幅であるため、結
露水の水滴は当該カバー材(6B)より張出した片側を
伝い落ることになるが、偏平チューブ(3)は全体がカ
バー材(6B)にて覆われた形になり、また該偏平チュ
ーブ(3)の表面に拡散したカバー材(6B)の成分が
犠牲防食材として機能するから、前記第一実施例と同様
に該偏平チューブ(3)は腐食劣化を生じにくく極めて
高い耐久性を発揮する。The heat exchanger of the second embodiment is used in an installed state in which the flow of air is in the direction shown by the arrow a in FIG. In this case, since the cover material (6B) has a width that covers the entire cutout (2) of the plate fin (1), the water droplets of the dew condensation will travel down one side of the cover material (6B). However, the flat tube (3) is entirely covered with the cover material (6B), and the component of the cover material (6B) diffused on the surface of the flat tube (3) functions as a sacrificial anticorrosion material. Thus, as in the first embodiment, the flat tube (3) hardly causes corrosion deterioration and exhibits extremely high durability.
【0020】第三実施例では、前記第一実施例における
カバー材(6A)に代えて図3(イ)に示すカバー材
(6C)を、また前記第二実施例におけるカバー材(6
B)に代えて図3(ロ)に示すカバー材(6D)を使用
する。これらカバー材(6C)(6D)は、寸法及び形
状的にはカバー材(6A)又は(6B)と同様である
が、外周面には幅方向に沿う多数の溝部(60)…がプレ
ートフィン(1)…の配列間隔に対応する間隔で設けて
ある。In the third embodiment, a cover material (6C) shown in FIG. 3A is used instead of the cover material (6A) in the first embodiment, and a cover material (6C) in the second embodiment is used.
A cover material (6D) shown in FIG. 3B is used instead of B). These cover members (6C) (6D) are similar in size and shape to the cover member (6A) or (6B), but have a large number of groove portions (60). (1) are provided at intervals corresponding to the arrangement intervals of.
【0021】従って、熱交換器のコア部(10)〔図4
(イ)参照〕の組立てに際し、各プレートフィン(1)
の切欠部(2)をカバー材(6C)(6D)の溝部(6
0)に嵌合させることにより、プレートフィン(1)…
を簡単に位置決めして正確に配列させることができる。
また得られる熱交換器は、プレートフィン(1)…とカ
バー材(6C)…又は(6D)…とが上記嵌合状態でロ
ウ付け接合された状態となるから、コア部(60)全体の
接合強度が大きく向上する。Therefore, the core part (10) of the heat exchanger [FIG.
(Refer to (a))] when assembling each plate fin (1)
Notch (2) of cover material (6C) (6D)
0), the plate fins (1) ...
Can be easily positioned and accurately arranged.
In the heat exchanger obtained, the plate fins (1) and the cover material (6C) or (6D) are brazed and joined in the above-mentioned fitting state, so that the entire core part (60) is joined. The joining strength is greatly improved.
【0022】なお、上記の第一〜第三実施例の熱交換器
は図4(イ)で示すように一対のヘッダー(4B)(4
B)がコア部(10)の両側に配置したタイプであるが、
この発明は、ヘッダー(4B)(4B)がなく、一本の
偏平チューブを一定長さで折り返す形に曲成した蛇行状
のサーペインタインチューブを用いた熱交換器にも同様
に適用できる。すなわち、この後者の熱交換器では、図
1〜図3で示す偏平チューブ(3)…がサーペインタイ
ンチューブの折り返しによる上下多段の直線部に相当す
ることになる。The heat exchanger of the first to third embodiments has a pair of headers (4B) (4B) as shown in FIG.
B) is the type arranged on both sides of the core part (10),
The present invention can be similarly applied to a heat exchanger using a serpentine tube, which has no headers (4B) and (4B) and is bent in a shape in which one flat tube is folded at a fixed length. That is, in the latter heat exchanger, the flat tubes (3) shown in FIGS. 1 to 3 correspond to the upper and lower multi-stage linear portions formed by folding back the serpentine tubes.
【0023】[0023]
【発明の効果】請求項1の発明によれば、垂直状態で左
右方向に配列したプレートフィンと、水平状態で上下多
段に配置した偏平チューブとでコア部を構成する熱交換
器として、偏平チューブの耐蝕性及び耐久性に優れ、し
かもプレートフィンと偏平チューブとを炉中ロウ付けに
て確実に接合一体化でき、またプレートフィンの強度を
確保できると共にそのルーバー加工に支障を生じないも
のが提供される。According to the first aspect of the present invention, a flat tube is used as a heat exchanger having a core portion composed of plate fins arranged vertically in the left-right direction and flat tubes arranged horizontally in multiple stages in a horizontal state. It is excellent in corrosion resistance and durability, and can securely join and integrate the plate fin and the flat tube by brazing in a furnace, and can secure the strength of the plate fin and do not hinder the louver processing. Is done.
【0024】請求項2の発明によれば、上記の熱交換器
として、偏平チューブの耐蝕性及び耐久性により優れる
ものが提供される。According to the second aspect of the present invention, there is provided the above-mentioned heat exchanger which is superior in corrosion resistance and durability of the flat tube.
【0025】請求項3の発明によれば、上記の熱交換器
として、コア部の組立てが容易であり、且つ該コア部全
体の接合強度に優れるものが提供される。According to the third aspect of the present invention, there is provided, as the above-mentioned heat exchanger, one which is easy to assemble a core portion and has excellent bonding strength of the entire core portion.
【図1】 この発明の熱交換器の第一実施例を示し、
(イ)図は組立て前のコア部の構成部材の斜視図、
(ロ)図は組立て後のコア部における要部の縦断側面図
である。FIG. 1 shows a first embodiment of a heat exchanger of the present invention,
(A) The figure is a perspective view of the components of the core before assembly,
(B) The figure is a longitudinal sectional side view of a main part of the core part after assembly.
【図2】 同第二実施例を示し、(イ)図は組立て前の
コア部の構成部材の斜視図、(ロ)図は組立て後のコア
部における要部の縦断側面図である。FIGS. 2A and 2B show the second embodiment, wherein FIG. 2A is a perspective view of components of a core unit before assembly, and FIG. 2B is a vertical sectional side view of a main part of the core unit after assembly.
【図3】 同第三実施例を示し、(イ)図及び(ロ)図
はカバー材の斜視図、(ハ)図は組立て後のコア部にお
ける要部の縦断正面図である。3 (a) and 3 (b) are perspective views of a cover member, and FIG. 3 (c) is a longitudinal sectional front view of a main part of a core part after assembly.
【図4】 コア部にプレートフィンと偏平チューブを用
いた熱交換器の構成例を示し、(イ)は熱交換器全体の
斜視図、(ロ)図はコア部における要部の縦断側面図で
ある。FIG. 4 shows a configuration example of a heat exchanger using a plate fin and a flat tube in a core portion, (a) is a perspective view of the entire heat exchanger, and (b) is a longitudinal sectional side view of a main portion in the core portion. It is.
【図5】 コア部にコルゲートフィンを用いた従来の熱
交換器の一例を示す正面図である。FIG. 5 is a front view showing an example of a conventional heat exchanger using corrugated fins for a core portion.
【図6】 コルゲートフィンを用いたコア部の水滴付着
状態を示し、(イ)図は偏平チューブが水平である場合
の要部の拡大正面図、(ロ)図は偏平チューブが垂直で
ある場合の要部の拡大正面図である。FIG. 6 shows a state of water droplets adhering to a core portion using a corrugated fin. FIG. 6A is an enlarged front view of a main part when the flat tube is horizontal, and FIG. 6B is a case where the flat tube is vertical. It is an enlarged front view of the principal part.
1・・・・・・・・プレートフィン 2・・・・・・・・切欠部 3・・・・・・・・偏平チューブ 6A〜6D・・・・カバー材 10・・・・・・・コア部 1 Plate fin 2 Notch 3 Flat tube 6A-6D Cover material 10 Core part
Claims (3)
列した多数枚のプレートフィンと、これらプレートフィ
ンの一側端より幅方向に凹入する切欠部に水平状態で嵌
入して上下多段に配置した偏平チューブとでコア部が構
成され、このコア部の偏平チューブ内を流れる熱交換媒
体と外部の空気との間で熱交換を行う熱交換器におい
て、 前記偏平チューブが、その一側端から上下面主要部を覆
う側面視略U字形のブレジングシート製のカバー材を介
して、前記プレートフィンの切欠部に嵌入されて当該プ
レートフィンと接合一体化してなることを特徴とする熱
交換器。1. A plurality of plate fins arranged at predetermined intervals in the left-right direction in a vertical state, and horizontally inserted into cutouts recessed in the width direction from one side end of the plate fins to form a plurality of vertical tiers. A core portion is constituted by the arranged flat tubes, and in a heat exchanger that exchanges heat between a heat exchange medium flowing in the flat tubes of the core portion and external air, the flat tubes have one end thereof. Characterized in that it is fitted into a notch of the plate fin through a cover material made of a brazing sheet having a substantially U-shape in a side view and covers the main part of the upper and lower surfaces, and is joined to and integrated with the plate fin. vessel.
ルミニウム系合金からなり、且つカバー材が偏平チュー
ブの合金材料よりも電位的に卑な合金材料である請求項
1記載の熱交換器。2. The heat exchanger according to claim 1, wherein the flat tube and the cover material are both made of an aluminum-based alloy, and the cover material is an alloy material having a potential lower than that of the flat tube.
フィンの周縁を嵌合させる溝部を有してなる請求項1又
は2に記載の熱交換器。3. The heat exchanger according to claim 1, further comprising a groove formed on an outer peripheral surface of the cover member to fit a peripheral edge of the plate fin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3827399A JP4105320B2 (en) | 1999-02-17 | 1999-02-17 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3827399A JP4105320B2 (en) | 1999-02-17 | 1999-02-17 | Heat exchanger |
Publications (3)
Publication Number | Publication Date |
---|---|
JP2000234883A true JP2000234883A (en) | 2000-08-29 |
JP2000234883A5 JP2000234883A5 (en) | 2006-03-16 |
JP4105320B2 JP4105320B2 (en) | 2008-06-25 |
Family
ID=12520713
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---|---|---|---|
JP3827399A Expired - Fee Related JP4105320B2 (en) | 1999-02-17 | 1999-02-17 | Heat exchanger |
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JP (1) | JP4105320B2 (en) |
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