JP2003075079A - Direct/alternating flow type cooling tower - Google Patents

Direct/alternating flow type cooling tower

Info

Publication number
JP2003075079A
JP2003075079A JP2002240067A JP2002240067A JP2003075079A JP 2003075079 A JP2003075079 A JP 2003075079A JP 2002240067 A JP2002240067 A JP 2002240067A JP 2002240067 A JP2002240067 A JP 2002240067A JP 2003075079 A JP2003075079 A JP 2003075079A
Authority
JP
Japan
Prior art keywords
pipe
cooling tower
meandering
straight
straight section
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2002240067A
Other languages
Japanese (ja)
Inventor
Jujiro Komiya
重次郎 小宮
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.)
Ebara Refrigeration Equipment and Systems Co Ltd
Original Assignee
Ebara Shinwa 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 Ebara Shinwa Ltd filed Critical Ebara Shinwa Ltd
Priority to JP2002240067A priority Critical patent/JP2003075079A/en
Publication of JP2003075079A publication Critical patent/JP2003075079A/en
Pending legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve heat exchange efficiency by eliminating a damage due to freezing of a zigzag pipe upon draining, and mounting many fins on the pipe of a straight section in a heat exchanger at a distance with a small pitch axially of the pipe of the straight section with ease. SOLUTION: Many vertically expandable fin members 13 are mounted over a pipe 12 of a straight section axially thereof with a small pitch at a distance, and a zigzag pipe 10 is installed hierarchically in a direct/alternating flow type cooling tower at a predetermined distance in the state where a flat plane involving the zigzag pipe 10 is inclined downward at the angle of about 2 to 3 degree with respect to a horizontal plane. The fin member 13 comprises a rectangular plate made of a synthetic resin flattened over the entire thereof, and through-holes, into and with which the pipe 12 of the straight section is inserted and brought into close contact, are formed in the rectangular plate in an equal interval with a predetermined pitch. Further, there is formed a slit section extendable radially of the pipe 12 of the straight section between the adjacent insertion holes in the assembled state to the zigzag pipe 10.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は直交流式冷却塔に関す
る。
BACKGROUND OF THE INVENTION The present invention relates to a cross-flow cooling tower.

【0002】[0002]

【従来の技術】この種のフイン付き密閉型熱交換器にお
ける蛇行管はU字形状の屈曲部で順次連なった直線部は
相互に平行に形成されている。従って蛇行面を殊に水平
方向に設置する場合、蛇行管の出入口の高さに若干の差
を設けて、この管内の排水を容易に行なえるようにして
設置している。また本件出願人は先に、屈曲部によって
連なる蛇行管において、各直線部の管が平行でなく、挟
角が30分乃至3度程度にしてある熱交換器を開発した
(実開昭63−190762号公報参照)が、直線部が
非平行なため、フィン材を取付けることは容易でなく、
もし取付けるとしてもコストを押し上げる原因になる。
2. Description of the Related Art In a meandering tube of this type of finned closed heat exchanger, straight portions which are successively connected by U-shaped bent portions are formed in parallel with each other. Therefore, when the meandering surface is installed horizontally, the height of the entrance and exit of the meandering pipe is slightly different so that the drainage in the pipe can be easily performed. In addition, the applicant of the present invention has previously developed a heat exchanger in which a straight tube in a meandering tube connected by a bent portion is not parallel, and the included angle is about 30 minutes to 3 degrees (actually 63- However, since the linear portions are non-parallel, it is not easy to attach the fin material.
Even if it is installed, it will increase the cost.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、個々の
直線部はそれぞれ完全に地表に対し、水平に設置される
ことになり、内部の液体を抜く場合でも、完全に抜け切
らず、若干の液体がどうしても蛇行管内に残る。また設
置後、何らかの外力により蛇行管が歪曲したときなど、
一部の直線部に液体が相当に残り、例えば水が残ったと
きは冬期や、寒冷地においては氷結して前記蛇行管を破
損しかねない。この発明は、叙上のような公知の欠点を
改善し、水抜きをしたときに、前記蛇行管内に液が残留
しないようにし、蛇行管の凍結による破損を解消すると
ともに、前記熱交換器における直線部の管に多数数枚の
フイン材を容易に前記直線部の管の軸線方向に小ピッチ
で間隔をおいて取付け、熱交換効率の向上の図った直交
流式冷却塔を提供することを目的とする。
However, the individual straight portions are installed completely horizontally with respect to the surface of the earth, and even if the liquid inside is drained, some liquid does not completely escape and some liquid remains. It will remain in the meandering tube. After installation, when the meandering tube is distorted by some external force,
A considerable amount of liquid may remain on some of the straight portions, for example, when water remains, it may freeze in the winter or in cold regions to damage the meandering pipe. This invention solves the above-mentioned known drawbacks, prevents liquid from remaining in the meandering pipe when draining water, eliminates breakage due to freezing of the meandering pipe, and eliminates the problems in the heat exchanger. It is possible to provide a cross-flow cooling tower with improved heat exchange efficiency by easily attaching a large number of fin materials to the straight pipe at a small pitch in the axial direction of the straight pipe. To aim.

【0004】[0004]

【課題を解決するための手段】前記課題を解決するため
に、特定発明は直交流式冷却塔内には蛇行管の直線部に
フインを多数設けたフイン付き熱交換器が間隔をおいて
階層的に多段に設けてあり、フイン付き熱交換器の供給
端には共通の供給ヘッダーが、またフイン付き熱交換器
の吐出端には共通の吐出ヘッダーが接続され、前記供給
端側は吐出端側より高位となる位置で接続され、前記フ
イン付き熱交換器における蛇行管の各屈曲部によって連
なる相隣る直線部の管が平行でなくその挾角が30分乃
至3度程度としてあり、これら直線部の管にわたり垂直
な伸縮可能なフイン材がその軸線方向に小ピッチで間隔
をおいて多数枚取り付けられ、前記蛇行管はこれらを含
む平面を水平面に対して2度乃至3度程度の傾斜角度で
下向きに傾斜させて設置されていることを特徴とする直
交流式冷却塔としてある。
In order to solve the above-mentioned problems, a specific invention is that a heat exchanger with fins having a large number of fins provided in a straight part of a meandering tube is arranged in a cross flow type cooling tower at intervals. The heat exchanger with fins has a common supply header connected to the supply end of the heat exchanger with fins, and the discharge end of the heat exchanger with fins has a common discharge header. The pipes of the linear parts which are connected at a position higher than the side and which are connected by the bent portions of the meandering pipe in the finned heat exchanger are not parallel to each other and the included angle is about 30 minutes to 3 degrees. A large number of vertically expandable fin materials are attached to the straight pipes at a small pitch in the axial direction, and the meandering pipe has a plane including them inclined by about 2 to 3 degrees with respect to the horizontal plane. Tilt down at an angle There the cross-flow cooling tower, characterized in that it is installed.

【0005】前記課題を解決するために、この発明の直
交流式冷却塔における前記フイン材は全体扁平な矩形板
から成り、前記直線部の管が挿入、密着される挿通孔が
等間隔に所定ピッチで前記矩形板に明けてあると共に、
隣接する前記挿通孔間には前記蛇行管への組み付け状態
において前記直線部の管の半径方向に拡張自在なスリッ
ト部が形成してあり、
In order to solve the above-mentioned problems, the fin material in the cross flow type cooling tower of the present invention is composed of a flat rectangular plate as a whole, and the insertion holes into which the straight pipes are inserted and adhered are predetermined at equal intervals. Along with opening the rectangular plate at a pitch,
Between the adjacent insertion holes, a slit portion that is expandable in the radial direction of the pipe of the linear portion is formed in the assembled state to the meandering pipe,

【0006】前記課題を解決するために、この発明の直
交流式冷却塔における前記スリット部は矩形板の横断方
向にこの上下縁までは達せず中央垂直な第1スリット
と、この第1スリットの両側に間隔を於いて上下から切
り込ませた第2スリットとで形成してなることが好まし
い。
In order to solve the above-mentioned problems, the slit portion in the cross flow type cooling tower of the present invention has a first slit which does not reach the upper and lower edges in the transverse direction of the rectangular plate and is central and vertical, and the first slit. It is preferably formed by a second slit which is cut from above and below with a space on both sides.

【0007】前記課題を解決するために、この発明の直
交流式冷却塔におけるフイン材は合成樹脂製としてあ
り、前記直線部の管の前記挾角に応じて前記直線部の管
の半径方向に拡張されて、前記直線部の管に固定されて
いる場合もある。
In order to solve the above-mentioned problems, the fin material in the cross flow type cooling tower of the present invention is made of synthetic resin, and the fin material is provided in the radial direction of the pipe of the straight part according to the included angle of the pipe of the straight part. It may be expanded and fixed to the straight tube.

【0008】前記課題を解決するために、この発明の直
交流式冷却塔における前記直交流式冷却塔における共通
の供給ヘッダーと吐出ヘッダーは同一側に位置し、前記
蛇行管を含む平面の傾斜角度は水平面に対して2度乃至
3度程度吐出側が低くしてあることもある。
In order to solve the above-mentioned problems, a common supply header and a common discharge header in the cross-flow cooling tower of the cross-flow cooling tower of the present invention are located on the same side, and the inclination angle of a plane including the meandering pipe is In some cases, the discharge side is lower by 2 to 3 degrees with respect to the horizontal plane.

【0009】[0009]

【実施例】実施例1 この実施例は請求項1乃至請求項4記載の発明の代表的
な実施例である。図1において、直交流式冷却塔におけ
る共通の供給ヘッダー15にフイン付き熱交換器20の
供給端が、またその共通の吐出ヘッダー16にフイン付
き熱交換器20の吐出端がそれぞれ、その供給端が吐出
端より高位となる位置で接続され、フイン付き密閉型熱
交換器20が前記直交流式冷却塔内に装填されてなり、
前記フイン付き密閉型熱交換器20における蛇行管10
の各屈曲部11によって連なる相隣る直線部の管12が
平行でなく、前記屈曲部11を挾む挾角θは30分乃至
3度、好ましくは37分〜50分程度としてある。また
屈曲部11の軸線の曲率半径R=管径d×xとして、x
=1.2乃至2としてある(図2参照)。一般にこの軸
線の曲率半径Rは直線部12が平行な従来技術のものよ
り小さい値とすることが好ましい。これら直線部の管1
2にわたり垂直な伸縮可能なフイン材13がその軸線方
向に小ピッチで間隔をおいて多数枚取り付けられ、前記
蛇行管10を含む平面を水平面に対して2度乃至3度程
度の傾斜角度αで下向きに傾斜させた状態で所定間隔を
おいて階層的に前記蛇行管10は前記直交流式冷却塔内
に設置されている。
Embodiment 1 This embodiment is a typical embodiment of the invention described in claims 1 to 4. In FIG. 1, the common feed header 15 of the cross-flow cooling tower has a feed end of the finned heat exchanger 20 and the common discharge header 16 has a feed end of the finned heat exchanger 20. Are connected at a position higher than the discharge end, and the finned closed heat exchanger 20 is loaded in the cross-flow cooling tower.
The meandering tube 10 in the finned closed heat exchanger 20.
The adjacent straight pipes 12 connected by the bent portions 11 are not parallel to each other, and the included angle θ between the bent portions 11 is 30 minutes to 3 degrees, preferably about 37 minutes to 50 minutes. In addition, the radius of curvature R of the axis of the bent portion 11 = tube diameter d × x, x
= 1.2 to 2 (see FIG. 2). In general, it is preferable that the radius of curvature R of this axis be smaller than that of the prior art in which the straight portions 12 are parallel. These straight tubes 1
A large number of vertically expandable fin members 13 are attached in the axial direction at a small pitch in the axial direction, and the plane including the meandering tube 10 is inclined at an angle α of about 2 to 3 degrees with respect to the horizontal plane. The meandering tubes 10 are installed in the cross flow type cooling tower in a hierarchical manner with a predetermined interval in a state of being inclined downward.

【0010】前記フイン材13は全体扁平な合成樹脂製
の矩形板から成り、前記各直線部の管12が挿入、密着
される挿通孔13aが等間隔に所定ピッチで前記矩形板
に明けてあると共に、隣接する前記挿通孔13a間には
前記蛇行管10への組み付け状態において前記直線部の
管12の半径方向に拡張自在なスリット部13bが形成
してある。
The fin member 13 is made of a rectangular flat plate made of a synthetic resin as a whole, and insertion holes 13a into which the tubes 12 of the respective straight portions are inserted and adhered are formed in the rectangular plate at equal intervals with a predetermined pitch. Along with the insertion holes 13a adjacent to each other, a slit portion 13b is formed which is expandable in the radial direction of the straight tube 12 when assembled to the meandering tube 10.

【0011】前記スリット部13bは矩形板の横断方向
にこの上下縁までは達せず中央垂直な第1スリット13
cと、この第1スリット13cの両側に間隔を於いて上
下から切り込ませた第2スリット13dとで形成してな
る(図3、図4参照)。
The slit portion 13b does not reach the upper and lower edges in the transverse direction of the rectangular plate, and the central first slit 13b is vertical.
c and a second slit 13d which is cut from above and below the first slit 13c with a space provided therebetween (see FIGS. 3 and 4).

【0012】前記フイン材13の組み付け方法の一例を
示せば、前記直線部の管12が前記挾角θに拡げられる
以前の相互平行な直線部の管12に前記挿通孔13aを
介して所定ピッチの間隔をおいて差し込み固定した後、
前記各屈曲部をなすUベント管を直線部の管端部にロー
付けして蛇行流路を形成した状態で、このUベント管の
付け根を支点として前記直線部の管12を前記挾角θ=
30分乃至3度に開くことに伴い、前記直線部の管12
の半径方向に拡張されて、前記フイン付き密閉型熱交換
管20を構成する。前記蛇行管10は銅、ステンレスス
チール、チタン合金など材質に特に制限はない。なお、
図1、図2に示す角α及びθは説明の都合上実際よりも
誇張して記載した。
An example of a method of assembling the fin member 13 will be described. The straight pipes 12 are parallel to the straight pipes 12 before being expanded to the included angle θ through the insertion holes 13a at a predetermined pitch. After inserting and fixing at intervals
In the state where the U-vent pipe forming each bent portion is brazed to the pipe end portion of the straight portion to form a meandering flow path, the straight-line portion of the straight-line portion 12 is used as a fulcrum to hold the flank angle θ. =
The tube 12 of the straight part is opened with opening for 30 minutes to 3 degrees.
And is expanded in the radial direction to form the finned closed heat exchange tube 20. There is no particular limitation on the material of the meandering tube 10 such as copper, stainless steel, and titanium alloy. In addition,
The angles α and θ shown in FIGS. 1 and 2 are exaggerated for convenience of description.

【0013】実施例2 この実施例は請求項5記載の発明の代表的な実施例であ
り、実施例1と異なる構成は、前記直交流式冷却塔にお
ける共通の供給ヘッダー15と吐出ヘッダー16は同一
側に位置し、吐出ヘッダー16に接続される前記蛇行管
10の傾斜角度βは水平面に対して2度乃至3度程度双
方のヘッダー15、16が低く傾斜させてある。即ち、
各蛇行管10の反対側が高位にある。その他、実施例1
と同一の符合は同一の構成を示し、同一の作用を為す
(図5参照)。
Embodiment 2 This embodiment is a typical embodiment of the invention described in claim 5, and is different from Embodiment 1 in that the common feed header 15 and discharge header 16 in the cross flow type cooling tower are The meandering pipe 10 located on the same side and connected to the discharge header 16 has an inclination angle β of about 2 to 3 degrees with respect to the horizontal plane, and both the headers 15 and 16 are inclined low. That is,
The opposite side of each serpentine tube 10 is at the higher position. Others, Example 1
The same reference numerals indicate the same configurations and perform the same operations (see FIG. 5).

【0014】[0014]

【効果】請求項1乃至5に記載された発明においては、
水抜きをしたときに、前記蛇行管内に液が残留しないよ
うにし、前記熱交換器における非平行の直線部の管に多
数数枚のフイン材が前記直線部の管の軸線方向に小ピッ
チで間隔をおいて取付けてあるから、熱交換効率を向上
できる。また前記の構造は前記挾角をなす相隣る直線部
の管間にわたり前記多数のフイン材をスリット部の拡張
により、これらを破損することなく組付け固定すること
ができる。また水抜き後は蛇行管内に水が残留せず、そ
の凍結による蛇行管の破損の破損はない。殊に請求項3
記載の発明においては、前記効果に加えて直線部の管の
間において前記中央垂直な第1スリットを前記屈曲部寄
りではその拡張度を小さく、この屈曲部から離れるにつ
れてこの拡張度を大きくでき、前記直線部の管にわたり
多数枚のフイン材を小ピッチで相隣る直線部の管の挾角
に対応して拡張した状態で垂直に並列配置でき、直交流
式冷却塔における散布水の冷却を促進できる。
According to the invention described in claims 1 to 5,
When water is drained, the liquid is prevented from remaining in the meandering pipe, and a number of fin materials are attached to the pipe of the non-parallel straight line portion in the heat exchanger at a small pitch in the axial direction of the straight line pipe. Since they are mounted at intervals, the heat exchange efficiency can be improved. Further, in the above-mentioned structure, the plurality of fin members can be assembled and fixed to each other without damaging them by expanding the slit portions between the pipes of the adjacent straight portions forming the included angle. Further, after draining water, water does not remain in the meandering pipe, and there is no damage of the meandering pipe due to the freezing. Especially claim 3
In the invention described, in addition to the effect, the central vertical first slit between the tubes of the straight portion is small in the degree of expansion near the bent portion, and the degree of expansion can be increased as the distance from the bent portion increases, A large number of fin materials can be arranged vertically in parallel with each other at a small pitch corresponding to the included angle of the straight-lined pipes over the straight-lined pipes, and the spray water can be cooled in the cross-flow cooling tower. Can be promoted.

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

【図1】フイン付き密閉型熱交換器の一例を示す平面図
である。
FIG. 1 is a plan view showing an example of a closed heat exchanger with fins.

【図2】図1のフインを省略したこの密閉型熱交換器を
ヘッダーに取付け使用する状態を示す斜視図である。
FIG. 2 is a perspective view showing a state in which the sealed heat exchanger without the fin of FIG. 1 is attached to a header and is used.

【図3】フイン材の拡張前の正面図である。FIG. 3 is a front view of the fin material before expansion.

【図4】図3のフイン材のスリット部を拡張した状態を
示す正面図である。
FIG. 4 is a front view showing a state in which a slit portion of the fin material of FIG. 3 is expanded.

【図5】図2と異なるヘッダーの配置を示す一部省略斜
視図である。
FIG. 5 is a partially omitted perspective view showing the arrangement of headers different from that in FIG.

【図6】図3に示すフイン材に直線部の管を相互平行に
挿通した状態を示す平面図である。
FIG. 6 is a plan view showing a state in which tubes of straight portions are inserted into the fin material shown in FIG. 3 in parallel with each other.

【符号の説明】[Explanation of symbols]

10 蛇行管 11 屈曲部 12 直線部分 13 フイン材 20 フイン付き密閉型熱交換器 θ 挾角 α 傾斜角 10 meandering tube 11 Bend 12 straight part 13 Fine wood Closed heat exchanger with 20 fins θ angle α inclination angle

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F28F 21/06 F28F 21/06 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) F28F 21/06 F28F 21/06

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】直交流式冷却塔内には蛇行管の直線部にフ
インを多数設けたフイン付き熱交換器が間隔をおいて階
層的に多段に設けてあり、フイン付き熱交換器の供給端
には共通の供給ヘッダーが、またフイン付き熱交換器の
吐出端には共通の吐出ヘッダーが接続され、前記供給端
側は吐出端側より高位となる位置で接続され、前記フイ
ン付き熱交換器における蛇行管の各屈曲部によって連な
る相隣る直線部の管が平行でなくその挾角が30分乃至
3度程度としてあり、これら直線部の管にわたり垂直な
伸縮可能なフイン材がその軸線方向に小ピッチで間隔を
おいて多数枚取り付けられ、 前記蛇行管はこれらを含む平面を水平面に対して2度乃
至3度程度の傾斜角度で下向きに傾斜させて設置されて
いることを特徴とする直交流式冷却塔。
1. A heat exchanger with fins, in which a large number of fins are provided in a straight line portion of a meandering tube, are arranged in a multi-tiered manner at intervals in a cross flow type cooling tower, and the heat exchanger with fins is supplied. A common supply header is connected to the end, and a common discharge header is connected to the discharge end of the heat exchanger with fins, the supply end side is connected at a position higher than the discharge end side, and the heat exchange with fins is connected. In the vessel, the pipes of the adjacent straight parts connected by the bent parts of the meandering pipe are not parallel to each other, and the included angle is about 30 minutes to 3 degrees. A plurality of meandering tubes are installed at a small pitch in the direction, and the meandering tube is installed such that a plane including the meandering tube is inclined downward at an inclination angle of about 2 to 3 degrees with respect to a horizontal plane. Cross flow type cooling tower.
【請求項2】前記フイン材は全体扁平な矩形板から成
り、前記直線部の管が挿入、密着される挿通孔が等間隔
に所定ピッチで前記矩形板に明けてあると共に、隣接す
る前記挿通孔間には前記蛇行管への組み付け状態におい
て前記直線部の管の半径方向に拡張自在なスリット部が
形成してあることを特徴とする請求項1記載の直交流式
冷却塔。
2. The fin member is made of a flat plate as a whole, and insertion holes into which the pipes of the straight line portion are inserted and adhered are opened at equal intervals in the rectangular plate, and the adjacent insertion plates are inserted. 2. The cross flow type cooling tower according to claim 1, wherein slits are formed between the holes so as to be expandable in a radial direction of the straight pipe in a state of being assembled to the meandering pipe.
【請求項3】前記スリット部は矩形板の横断方向にこの
上下縁までは達せず中央垂直な第1スリットと、この第
1スリットの両側に間隔を於いて上下から切り込ませた
第2スリットとで形成してなることを特徴とする請求項
2記載の直交流式冷却塔。
3. The slit portion is a first slit which does not reach the upper and lower edges in the transverse direction of the rectangular plate and is perpendicular to the center, and a second slit which is cut from the upper and lower sides at intervals on both sides of the first slit. The cross-flow cooling tower according to claim 2, which is formed by
【請求項4】フイン材は合成樹脂製としてあり、前記直
線部の管の前記挾角に応じて前記直線部の管の半径方向
に拡張されて、前記直線部の管に固定されていることを
特徴とする請求項1、2または3記載の直交流式冷却
塔。
4. The fin material is made of synthetic resin, and is expanded in the radial direction of the straight section pipe in accordance with the included angle of the straight section tube and is fixed to the straight section tube. The cross-flow cooling tower according to claim 1, 2, or 3.
【請求項5】前記直交流式冷却塔における共通の供給ヘ
ッダーと吐出ヘッダーは同一側に位置し、前記蛇行管を
含む平面の傾斜角度は水平面に対して2度乃至3度程度
吐出側が低くしてあることを特徴とする請求項1、2、
3または4記載の直交流式冷却塔。
5. The common feed header and discharge header in the cross flow type cooling tower are located on the same side, and the inclination angle of the plane including the meandering pipe is set to be lower by 2 to 3 degrees with respect to the horizontal plane on the discharge side. Claims 1 and 2, characterized in that
The cross-flow cooling tower according to 3 or 4.
JP2002240067A 2002-08-21 2002-08-21 Direct/alternating flow type cooling tower Pending JP2003075079A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002240067A JP2003075079A (en) 2002-08-21 2002-08-21 Direct/alternating flow type cooling tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002240067A JP2003075079A (en) 2002-08-21 2002-08-21 Direct/alternating flow type cooling tower

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP23715693A Division JPH0771894A (en) 1993-08-31 1993-08-31 Manufacture of finned hermetic heat exchanger

Publications (1)

Publication Number Publication Date
JP2003075079A true JP2003075079A (en) 2003-03-12

Family

ID=19196443

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002240067A Pending JP2003075079A (en) 2002-08-21 2002-08-21 Direct/alternating flow type cooling tower

Country Status (1)

Country Link
JP (1) JP2003075079A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008091738A1 (en) * 2007-01-23 2008-07-31 Modine Manufacturing Company Heat exchanger and method
JP2015121402A (en) * 2015-04-01 2015-07-02 パナソニックIpマネジメント株式会社 Cooling device, electronic apparatus loading the same, and electric car
CN107923712A (en) * 2015-08-14 2018-04-17 开利公司 Micro-channel heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008091738A1 (en) * 2007-01-23 2008-07-31 Modine Manufacturing Company Heat exchanger and method
US7921904B2 (en) 2007-01-23 2011-04-12 Modine Manufacturing Company Heat exchanger and method
JP2015121402A (en) * 2015-04-01 2015-07-02 パナソニックIpマネジメント株式会社 Cooling device, electronic apparatus loading the same, and electric car
CN107923712A (en) * 2015-08-14 2018-04-17 开利公司 Micro-channel heat exchanger

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