JP2008008585A - Tube for heat exchanger - Google Patents

Tube for heat exchanger Download PDF

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JP2008008585A
JP2008008585A JP2006181767A JP2006181767A JP2008008585A JP 2008008585 A JP2008008585 A JP 2008008585A JP 2006181767 A JP2006181767 A JP 2006181767A JP 2006181767 A JP2006181767 A JP 2006181767A JP 2008008585 A JP2008008585 A JP 2008008585A
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inner fin
communication holes
heat exchanger
interval
longitudinal direction
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JP2006181767A
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Japanese (ja)
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Masatake Niihama
正剛 新濱
Seiko Sogabe
誠広 曽我部
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Marelli Corp
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Calsonic Kansei Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a tube for a heat exchanger, which easily sets the optimum interval of communication holes of an inner fin, and favorably fixes a holding part and the inner fin by brazing. <P>SOLUTION: The tube 1 for heat exchangers is provided with: a flat tube like holder part 2; the corrugated inner fin 3 housed in the holder part 2 and forming a plurality of circulation medium passages 4 extending in a longitudinal direction of the holder part 2; and a plurality of communication holes 5 mutually communicated with adjacent circulation medium passages 4 of the inner fin 3 and arranged at a predetermined interval in a longitudinal direction of the inner fin 3. Each communication hole 5 is formed astride at least two crests of the inner fin 3, and it is formed like an obliquely crossing slit with respect to the circulation medium passage 4. In the inner fin 3, when the interval between the communication holes 5 is L mm, a width is W mm, a clad ratio is R%, and a thickness is T mm, a brazing index Z=L×W×R×T/100≥0.77. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、熱交換器用チューブに関する。   The present invention relates to a heat exchanger tube.

従来、偏平管状のホルダ部と、ホルダ部内に収容され、且つ、該ホルダ部の長さ方向へ延びる複数の流通媒体通路を形成する波板状のインナーフィンと、インナーフィンの隣り合う流通媒体通路を互いに連通し、且つ、インナーフィンの長手方向へ所定間隔で配置された複数の連通孔を備え、各連通孔が、インナーフィンの波の頂部の少なくとも二つにまたがると共に、流通媒体通路に対して斜交するスリット状に形成された熱交換器用チューブの技術が公知になっている(特許文献1参照)。
特開2004−61065号公報
Conventionally, a flat tubular holder part, a corrugated inner fin that is accommodated in the holder part and forms a plurality of circulation medium paths extending in the length direction of the holder part, and a circulation medium path adjacent to the inner fin And a plurality of communication holes arranged at predetermined intervals in the longitudinal direction of the inner fin, each communication hole spans at least two of the wave fins of the inner fin, The technology of a heat exchanger tube formed into a slanting slit shape is known (see Patent Document 1).
JP 2004-61065 A

しかしながら、従来の熱交換器用チューブにおいて、各連通孔の間隔を小さくすると、熱交換器用チューブを仮組みした際にインナーフィンがホルダ部の加圧によって座屈し、この結果、インナーフィンの一部がホルダ部と非接触状態となってろう付け不良が発生するという問題点があった。
加えて、インナーフィンの連通孔でフラックスの流動が多数の箇所で分断されて十分に充填されず、ホルダ部との間に良好なフィレットを形成してろう付け固定できないという問題点があった。
一方、各連通孔の間隔を大きくすると、連通孔の効果をあまり期待できず、インナーフィンの連通孔の最適な間隔を容易に設定したいという要求があった。
However, in the conventional heat exchanger tube, if the interval between the communication holes is reduced, the inner fin is buckled by pressurization of the holder portion when the heat exchanger tube is temporarily assembled, and as a result, a part of the inner fin is There was a problem that a poor brazing occurred due to contact with the holder portion.
In addition, there is a problem in that the flux flow is divided at a large number of locations at the inner fin communication holes and is not sufficiently filled, and a good fillet cannot be formed between the holder and brazed.
On the other hand, if the interval between the communication holes is increased, the effect of the communication hole cannot be expected so much, and there has been a demand to easily set the optimal interval between the communication holes of the inner fin.

本発明は上記課題を解決するためになされたものであって、その目的とするところは、インナーフィンの連通孔の最適な間隔を容易に設定でき、ホルダ部とインナーフィンを良好にろう付け固定できる熱交換器用チューブを提供することである。   The present invention has been made to solve the above-described problems, and the object of the present invention is to easily set the optimal interval between the communication holes of the inner fin, and to fix the holder portion and the inner fin by brazing well. It is to provide a heat exchanger tube.

本発明の請求項1記載の発明では、偏平管状のホルダ部と、前記ホルダ部内に収容され、且つ、該ホルダ部の長手方向へ延びる複数の流通媒体通路を形成する波板状のインナーフィンと、前記インナーフィンの隣り合う流通媒体通路を互いに連通し、且つ、インナーフィンの長手方向へ所定間隔で配置された複数の連通孔を備え、前記各連通孔が、インナーフィンの波の頂部の少なくとも二つにまたがると共に、流通媒体通路に対して斜交するスリット状に形成された熱交換器用チューブにおいて、前記インナーフィンにおける連通孔の間隔をL(mm)、幅をW(mm)、クラッド率をR(%)、板厚(mm)をTとした場合に、ろう付け指数Z=L×W×R×T/100≧0.77としたことを特徴とする。   According to a first aspect of the present invention, a flat tubular holder portion, and corrugated inner fins that are accommodated in the holder portion and that form a plurality of flow medium passages extending in the longitudinal direction of the holder portion, A plurality of communication holes communicating with each other of the adjacent distribution medium passages of the inner fins and arranged at predetermined intervals in the longitudinal direction of the inner fins, wherein each of the communication holes is at least a wave top of the inner fin. In the heat exchanger tube formed in a slit shape that crosses the two and is oblique to the flow medium passage, the interval between the communication holes in the inner fin is L (mm), the width is W (mm), and the cladding ratio Is R (%) and the plate thickness (mm) is T, the brazing index Z = L × W × R × T / 100 ≧ 0.77.

本発明の請求項1記載の発明にあっては、偏平管状のホルダ部と、前記ホルダ部内に収容され、且つ、該ホルダ部の長手方向へ延びる複数の流通媒体通路を形成する波板状のインナーフィンと、前記インナーフィンの隣り合う流通媒体通路を互いに連通し、且つ、インナーフィンの長手方向へ所定間隔で配置された複数の連通孔を備え、前記各連通孔が、インナーフィンの波の頂部の少なくとも二つにまたがると共に、流通媒体通路に対して斜交するスリット状に形成された熱交換器用チューブにおいて、前記インナーフィンにおける連通孔の間隔をL(mm)、幅をW(mm)、クラッド率をR(%)、板厚(mm)をTとした場合に、ろう付け指数Z=L×W×R×T/100≧0.77としたため、インナーフィンの連通孔の最適な間隔を容易に設定でき、ホルダ部とインナーフィンを良好にろう付け固定できる。   According to the first aspect of the present invention, the flat tubular holder portion and the corrugated plate-like member that is accommodated in the holder portion and that forms a plurality of flow medium passages extending in the longitudinal direction of the holder portion. Inner fins and a plurality of communication holes that communicate with each other between adjacent inner passages of the inner fins and are arranged at predetermined intervals in the longitudinal direction of the inner fins, and each of the communication holes includes a wave of the inner fin. In the heat exchanger tube formed in a slit shape that spans at least two of the top portions and obliquely crosses the flow medium passage, the interval between the communication holes in the inner fin is L (mm), and the width is W (mm) When the cladding rate is R (%) and the plate thickness (mm) is T, the brazing index Z = L × W × R × T / 100 ≧ 0.77, so that the inner fin communication hole is optimal. interval Easily set, the holder portion and the inner fin can be satisfactorily brazed.

以下、この発明の実施例を図面に基づいて説明する。   Embodiments of the present invention will be described below with reference to the drawings.

以下、実施例1を説明する。
図1は本発明の実施例1の熱交換器用チューブを示す斜視図、図2は本実施例1の熱交換器用チューブの内部を説明する断面図、図3はインナーフィンの側面図(a)と平面図(b)、図4は本実施例1の熱交換器用チューブの製造を説明する図である。
Example 1 will be described below.
1 is a perspective view showing a heat exchanger tube according to a first embodiment of the present invention, FIG. 2 is a cross-sectional view illustrating the inside of the heat exchanger tube according to the first embodiment, and FIG. 3 is a side view of an inner fin (a). FIG. 4 is a plan view (b) and FIG. 4 are diagrams for explaining the manufacture of the heat exchanger tube of the first embodiment.

先ず、全体構成を説明する。
図1、2に示すように、本実施例1の熱交換器用チューブ1は、偏平管状のホルダ部2と、このホルダ部2の内部に収容された波板状のインナーフィン3が備えられている。
First, the overall configuration will be described.
As shown in FIGS. 1 and 2, the heat exchanger tube 1 according to the first embodiment includes a flat tubular holder portion 2 and a corrugated inner fin 3 housed in the holder portion 2. Yes.

ホルダ部2は、所定間隔をおいて互いに対向する一対の平坦部2a,2bと、これら両平坦部2a,2bの一方の幅方向端部を一体的に接続する屈曲部2cと、一対の平坦部2a,2bの他方の幅方向端部側にそれぞれ形成された接合部2d,2eを有して偏平管状に形成される他、これら両接合部2d,2e同士は互いに当接した状態で接合されている。
なお、本実施例1の各接合部2d,2eはホルダ部2の幅方向両端部がそれぞれ内側に巻き締められてその外周の一部が接合されているが、この限りではない。
The holder portion 2 includes a pair of flat portions 2a and 2b that face each other at a predetermined interval, a bent portion 2c that integrally connects one width direction end portions of the both flat portions 2a and 2b, and a pair of flat portions. The joints 2d and 2e are formed in a flat tube shape with joints 2d and 2e formed on the other widthwise end of the parts 2a and 2b, and the joints 2d and 2e are joined in contact with each other. Has been.
In addition, as for each joining part 2d and 2e of the present Example 1, the both ends of the width direction of the holder part 2 are respectively wound inside, and a part of the outer periphery is joined, but it is not this limitation.

インナーフィン3は、山3aと谷3bが交互に配置される波板状に形成される他、各山3aが平坦部2aの内面に、各谷3bが平坦部2bの内面にそれぞれ接合され、これによって、ホルダ部2の長手方向へ延びる複数の流通媒体通路4が形成されている。   The inner fin 3 is formed in a corrugated shape in which peaks 3a and valleys 3b are alternately arranged, each peak 3a is joined to the inner surface of the flat portion 2a, and each valley 3b is joined to the inner surface of the flat portion 2b, Thereby, a plurality of distribution medium passages 4 extending in the longitudinal direction of the holder portion 2 are formed.

さらに、図3に示すように、インナーフィン3には、山3aと谷3bによって形成される波の頂部の少なくとも2つにまたがると共に、インナーフィン3の長手方向(流通媒体通路4の長手方向でもある)に対して斜交するスリット状に形成された複数の連通孔5がインナーフィン3の長手方向へ後述する所定間隔Lで千鳥状に配置されている。
なお、連通孔5の流通媒体通路4に対する傾斜角度は40°〜60°程度が好ましい。
Furthermore, as shown in FIG. 3, the inner fin 3 extends over at least two of the tops of the waves formed by the peaks 3 a and the valleys 3 b, and the longitudinal direction of the inner fin 3 (even in the longitudinal direction of the distribution medium passage 4). A plurality of communication holes 5 formed in a slit shape obliquely intersecting with each other are arranged in a staggered manner in the longitudinal direction of the inner fin 3 at a predetermined interval L described later.
The inclination angle of the communication hole 5 with respect to the flow medium passage 4 is preferably about 40 ° to 60 °.

そして、インナーフィン3における連通孔5の間隔をL(mm)、幅をW(mm)、クラッド率をR(%)、板厚(mm)をTとした場合に、ろう付け指数Z=L×W×R×T/100≧0.77となるように上記L、W、R、Tの値がそれぞれ設定されている。
なお、本実施例1では、L=15.00(mm)、W=25.66mm、R=10(%)、T=0.06(mm)となっている。
When the interval between the communication holes 5 in the inner fin 3 is L (mm), the width is W (mm), the cladding rate is R (%), and the plate thickness (mm) is T, the brazing index Z = L The values of L, W, R, and T are set so that × W × R × T / 100 ≧ 0.77.
In the first embodiment, L = 15.00 (mm), W = 25.66 mm, R = 10 (%), and T = 0.06 (mm).

その他、熱交換器用チューブ1の各構成部材は、全てアルミ製であり、インナーフィン3の外周面には上記クラッド率Rでクラッド材が設けられる他、ホルダ部2の外周面にもクラッド材が設けられている。   In addition, the constituent members of the heat exchanger tube 1 are all made of aluminum, and the clad material is provided on the outer circumferential surface of the inner fin 3 at the clad rate R, and the clad material is also disposed on the outer circumferential surface of the holder portion 2. Is provided.

このように構成された熱交換器用チューブ1を製造する際には、図4に示すように、接合部2d,2eが拡開されたホルダ部2の内側にインナーフィン3を配置した状態とし、これら接合部2d,2e同士を重ね合わせると共に、両平坦部2a,2bでインナーフィン3のそれぞれ対応する各山3aと各谷3bを加圧して仮組みする。   When manufacturing the heat exchanger tube 1 configured in this way, as shown in FIG. 4, the inner fins 3 are arranged inside the holder portion 2 where the joint portions 2d and 2e are expanded, The joint portions 2d and 2e are overlapped with each other, and the flat portions 2a and 2b are temporarily assembled by pressing the corresponding peaks 3a and valleys 3b of the inner fin 3 respectively.

次に、上記仮組みされた熱交換器用チューブ1を複数本用意し、図外のチューブプレートやフィン等と共に仮組みして熱交換器のコア部を形成した後、図外の加熱炉に搬送して熱処理することにより、各構成部材の接合部位を一体的にろう付け固定する。   Next, a plurality of the above-prepared heat exchanger tubes 1 are prepared, and temporarily assembled together with tube plates, fins, etc. not shown to form the core portion of the heat exchanger, and then transferred to a heating furnace not shown. Then, by heat treatment, the joint portions of the constituent members are integrally brazed and fixed.

このように構成された熱交換器用チューブ1は、その一端側が図外の熱交換器の上流側のタンクに連通接続される一方、その他端側が図外の熱交換器の下流側のタンクに連通接続される。   One end of the heat exchanger tube 1 configured in this way is connected to the upstream tank of the heat exchanger (not shown), and the other end is connected to the downstream tank of the heat exchanger (not shown). Connected.

そして、上流側のタンクの流通媒体が、各熱交換器用チューブ1の流通媒体通路4を介して下流側のタンクへ流入する間に、コア部を通過する外気と熱交換することにより冷却される。
この際、インナーフィン3は上記熱交換を促進すると共に、流通媒体の一部が連通孔5を介して隣接する流通媒体通路4同士間を流通し、これによって流通媒体を乱流化して上記熱交換を促進できる。
Then, while the flow medium in the upstream tank flows into the downstream tank via the flow medium passage 4 of each heat exchanger tube 1, it is cooled by exchanging heat with the outside air passing through the core portion. .
At this time, the inner fin 3 promotes the heat exchange, and a part of the circulation medium circulates between the circulation medium passages 4 adjacent to each other through the communication holes 5, thereby turbulently circulating the circulation medium and Exchange can be promoted.

ここで、従来の発明にあっては、各連通孔の間隔を小さくすると、熱交換器用チューブを仮組みした際にインナーフィンがホルダ部の加圧によって座屈し、この結果、インナーフィンの一部がホルダ部と非接触状態となってろう付け不良が発生するという問題点があった。
加えて、インナーフィンの連通孔でフラックスの流動が多数の箇所で分断されて十分に充填されず、ホルダ部との間に良好なフィレットを形成してろう付け固定できないという問題点があった。
Here, in the conventional invention, when the interval between the communication holes is reduced, the inner fin is buckled by the pressurization of the holder portion when the heat exchanger tube is temporarily assembled, and as a result, a part of the inner fin However, there is a problem in that brazing failure occurs due to contact with the holder portion.
In addition, there is a problem in that the flux flow is divided at a large number of locations at the inner fin communication holes and is not sufficiently filled, and a good fillet cannot be formed between the holder and brazed.

そこで、幅W=25.66mm、クラッド率R=10%、板厚T=0.06mmとした熱交換器用チューブの連通孔5の間隔Lを4.00mmから徐々に大きくした複数種類の熱交換器用チューブを用意し、それぞれろう付けして試験を行った結果、連通孔5の間隔Lが5.00mm以上、つまり、ろう付け指数Z=L×W×R×T/100≧0.77(正確にはZ≧0.7698)とした場合に、インナーフィン3の座屈を招くことなく熱交換器チューブを仮組みでき、さらに、ホルダ部2とインナーフィン3を良好にろう付け固定できることを確認した。
さらに、上記Lの値を増減しつつ、W、R、Tを実際上の製品として設計変更可能な範囲内で様々な値に代えた場合も同様の結果となった。
なお、Lをあまり大きくすると、連通孔5の形成数が減る上、連通孔5による効果を得られないため、実際上の製品としては、Z≦8.4とすることが好ましい。
Therefore, a plurality of types of heat exchange in which the interval L between the communication holes 5 of the heat exchanger tube having a width W = 25.66 mm, a cladding rate R = 10%, and a plate thickness T = 0.06 mm is gradually increased from 4.00 mm. As a result of preparing test tubes and brazing each, the interval L of the communication holes 5 was 5.00 mm or more, that is, brazing index Z = L × W × R × T / 100 ≧ 0.77 ( To be precise, when Z ≧ 0.7698), the heat exchanger tube can be temporarily assembled without causing buckling of the inner fin 3, and furthermore, the holder part 2 and the inner fin 3 can be satisfactorily brazed and fixed. confirmed.
Furthermore, the same result was obtained when W, R, and T were changed to various values within a range in which the design could be changed as an actual product while increasing or decreasing the value of L.
If L is too large, the number of communication holes 5 formed is reduced and the effect of the communication holes 5 cannot be obtained. Therefore, as an actual product, it is preferable that Z ≦ 8.4.

従って、インナーフィン3の連通孔5の間隔をL(mm)、幅をW(mm)、クラッド率をR(%)、板厚(mm)をTとした場合に、ろう付け指数Z=L×W×R×T/100≧0.77となるように連通孔5の間隔Lを設定することにより、インナーフィン3の連通孔5の最適な間隔を容易に設定でき、ホルダ部2とインナーフィン3を良好にろう付け固定できる。   Accordingly, when the interval between the communication holes 5 of the inner fin 3 is L (mm), the width is W (mm), the cladding ratio is R (%), and the plate thickness (mm) is T, the brazing index Z = L By setting the interval L of the communication holes 5 so that × W × R × T / 100 ≧ 0.77, the optimal interval of the communication holes 5 of the inner fin 3 can be easily set, and the holder portion 2 and the inner The fin 3 can be brazed and fixed satisfactorily.

また、連通孔5の間隔Lを予め決定しておき、幅W、クラッド率R、板厚Tについて最適な値を検討し対応することもできる。ただし、クラッド率Rは15%以下の値に設定するのが好ましい。   Further, the interval L between the communication holes 5 can be determined in advance, and optimum values for the width W, the cladding ratio R, and the plate thickness T can be examined and dealt with. However, the cladding ratio R is preferably set to a value of 15% or less.

次に、効果を説明する。
以上、説明したように、本実施例1の熱交換器用チューブ1にあっては、偏平管状のホルダ部2と、ホルダ部2内に収容され、且つ、該ホルダ部2の長手方向へ延びる複数の流通媒体通路4を形成する波板状のインナーフィン3と、インナーフィン3の隣り合う流通媒体通路4を互いに連通し、且つ、インナーフィン3の長手方向へ所定間隔で配置された複数の連通孔5を備え、各連通孔5が、インナーフィン3の波の頂部の少なくとも二つにまたがると共に、流通媒体通路4に対して斜交するスリット状に形成された熱交換器用チューブ1において、インナーフィン3における連通孔5の間隔をL(mm)、幅をW(mm)、クラッド率をR(%)、板厚(mm)をTとした場合に、ろう付け指数Z=L×W×R×T/100≧0.77としたため、インナーフィン3の連通孔5の最適な間隔を容易に設定でき、ホルダ部とインナーフィン3を良好にろう付け固定できる。
Next, the effect will be described.
As described above, in the heat exchanger tube 1 of the first embodiment, a flat tubular holder portion 2 and a plurality of holder portions 2 accommodated in the holder portion 2 and extending in the longitudinal direction of the holder portion 2. The inner fins 3 in the form of corrugated plates forming the circulation medium passages 4 and the circulation medium passages 4 adjacent to the inner fins 3 communicate with each other, and a plurality of communications are arranged at predetermined intervals in the longitudinal direction of the inner fins 3. In the heat exchanger tube 1 provided with holes 5, each communication hole 5 extending over at least two of the wave tops of the inner fins 3 and obliquely formed with respect to the circulation medium passage 4, Brazing index Z = L × W × where L is the distance between the communication holes 5 in the fin 3, W is the width (mm), R (%) is the cladding ratio, and T is the thickness (mm). R × T / 100 ≧ 0.77 Therefore, the optimal spacing of the communicating hole 5 of the inner fin 3 can be easily set, the holder portion and the inner fin 3 can be satisfactorily brazed.

以上、本実施例を説明してきたが、本発明は上述の実施例に限られるものではなく、本発明の要旨を逸脱しない範囲の設計変更等があっても、本発明に含まれる。
例えば、連通孔5は、インナーフィン3の山3aの少なくとも二つにまたがると共に、流通媒体通路4に対して斜交するスリット状に形成されていれば良く、図5に示すように、車幅方向に長い連通孔10を形成しても良い。
Although the present embodiment has been described above, the present invention is not limited to the above-described embodiment, and design changes and the like within a scope not departing from the gist of the present invention are included in the present invention.
For example, the communication hole 5 only needs to be formed in a slit shape that extends over at least two of the peaks 3a of the inner fin 3 and obliquely intersects with the distribution medium passage 4. As shown in FIG. You may form the communication hole 10 long in a direction.

本発明の実施例1の熱交換器用チューブを示す斜視図である。It is a perspective view which shows the tube for heat exchangers of Example 1 of this invention. 本実施例1の熱交換器用チューブの内部を説明する断面図である。It is sectional drawing explaining the inside of the tube for heat exchangers of the present Example 1. FIG. インナーフィンの側面図(a)と平面図(b)である。It is the side view (a) and top view (b) of an inner fin. 本実施例1の熱交換器用チューブの製造を説明する図である。It is a figure explaining manufacture of the tube for heat exchangers of the present Example 1. FIG. その他の実施例の熱交換器用チューブを説明する図である。It is a figure explaining the tube for heat exchangers of another Example.

符号の説明Explanation of symbols

1 熱交換器用チューブ
2 ホルダ部
2a、2b 平坦部
2c 屈曲部
2d、2e 接合部
3 インナーフィン
3a 山
3b 谷
4 流通媒体通路
5 連通孔
DESCRIPTION OF SYMBOLS 1 Heat exchanger tube 2 Holder part 2a, 2b Flat part 2c Bending part 2d, 2e Joint part 3 Inner fin 3a Mountain 3b Valley 4 Distribution medium channel | path 5 Communication hole

Claims (1)

偏平管状のホルダ部と、
前記ホルダ部内に収容され、且つ、該ホルダ部の長手方向へ延びる複数の流通媒体通路を形成する波板状のインナーフィンと、
前記インナーフィンの隣り合う流通媒体通路を互いに連通し、且つ、インナーフィンの長手方向へ所定間隔で配置された複数の連通孔を備え、
前記各連通孔が、インナーフィンの波の頂部の少なくとも二つにまたがると共に、流通媒体通路に対して斜交するスリット状に形成された熱交換器用チューブにおいて、
前記インナーフィンにおける連通孔の間隔をL(mm)、幅をW(mm)、クラッド率をR(%)、板厚(mm)をTとした場合に、
ろう付け指数Z=L×W×R×T/100≧0.77
としたことを特徴とする熱交換器用チューブ。
A flat tubular holder,
A corrugated inner fin that is accommodated in the holder part and forms a plurality of flow medium passages extending in the longitudinal direction of the holder part;
A plurality of communication holes arranged at predetermined intervals in the longitudinal direction of the inner fins, and the communication medium passages adjacent to each other of the inner fins communicate with each other;
Each of the communication holes spans at least two of the tops of the waves of the inner fin, and in the heat exchanger tube formed in a slit shape obliquely with respect to the circulation medium passage,
When the interval between the communication holes in the inner fin is L (mm), the width is W (mm), the cladding rate is R (%), and the plate thickness (mm) is T,
Brazing index Z = L × W × R × T / 100 ≧ 0.77
A heat exchanger tube characterized by the above.
JP2006181767A 2006-06-30 2006-06-30 Tube for heat exchanger Withdrawn JP2008008585A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006181767A JP2008008585A (en) 2006-06-30 2006-06-30 Tube for heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006181767A JP2008008585A (en) 2006-06-30 2006-06-30 Tube for heat exchanger

Publications (1)

Publication Number Publication Date
JP2008008585A true JP2008008585A (en) 2008-01-17

Family

ID=39066956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006181767A Withdrawn JP2008008585A (en) 2006-06-30 2006-06-30 Tube for heat exchanger

Country Status (1)

Country Link
JP (1) JP2008008585A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102345995A (en) * 2010-08-03 2012-02-08 株式会社电装 Condenser

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102345995A (en) * 2010-08-03 2012-02-08 株式会社电装 Condenser
US9121629B2 (en) 2010-08-03 2015-09-01 Denso Corporation Condenser

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