JPH11211367A - Waveform heat transfer unit and heat exchanger - Google Patents

Waveform heat transfer unit and heat exchanger

Info

Publication number
JPH11211367A
JPH11211367A JP3217498A JP3217498A JPH11211367A JP H11211367 A JPH11211367 A JP H11211367A JP 3217498 A JP3217498 A JP 3217498A JP 3217498 A JP3217498 A JP 3217498A JP H11211367 A JPH11211367 A JP H11211367A
Authority
JP
Japan
Prior art keywords
heat transfer
liquid
transfer unit
waveform
header
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
JP3217498A
Other languages
Japanese (ja)
Inventor
Junji Ashikaga
純司 足利
Kazuo Kitahara
上雄 北原
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.)
Kyushu Electric Power Co Inc
Toshiba Plant Construction Corp
Original Assignee
Kyushu Electric Power Co Inc
Toshiba Plant Construction Corp
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 Kyushu Electric Power Co Inc, Toshiba Plant Construction Corp filed Critical Kyushu Electric Power Co Inc
Priority to JP3217498A priority Critical patent/JPH11211367A/en
Publication of JPH11211367A publication Critical patent/JPH11211367A/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 enhance a heat transfer efficiency by connecting a pair of parallel waveform plates at an interval to diffuse a liquid to be introduced between the plates by a capillary, thereby increasing a heat transfer area per liquid volume between the plates. SOLUTION: A liquid flowing part 3 has a pipe-like header 3a made of a similar material to a waveform plate 2, and a communicating part 3b for communicating the header 3a with a waveform heat transfer unit 1. A liquid 20 to be supplied to the header 3a is introduced into the unit 1 via the part 3b. A liquid flowing-out part also has a pipe-like header similar to the part 3, and a communicating part for communicating the header within the unit 1. The liquid flowing out from the unit 1 is introduced into the header via the communicating part, and discharged. Thus, a content stayed in the plate 2 is reduced, and a heat transfer area per liquid volume is increased.

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】本発明は熱交換器に用いられ
る波形伝熱ユニット、およびその波形伝熱ユニットを複
数並行に配置して構成される熱交換器に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a corrugated heat transfer unit used in a heat exchanger and a heat exchanger constituted by arranging a plurality of the corrugated heat transfer units in parallel.

【0002】[0002]

【従来の技術】液体−液体間または液体−気体間で熱交
換をする熱交換器として、多管式、二重管式、滴下式ま
たはプレート式などの形式がある。これらの中でプレー
ト式は小型化が可能であること、熱交換効率が高いこと
などの理由から多くの分野で採用されている。従来のプ
レート式熱交換器としては、例えば多数の波形プレート
を所定間隔で整列し、各波形プレート間に液体とそれと
熱交換すべき他の液体または気体などの流体を交互に通
過させるように構成したものがある。
2. Description of the Related Art As a heat exchanger for exchanging heat between liquid and liquid or between liquid and gas, there are a multi-tube type, a double-tube type, a dropping type, a plate type and the like. Among them, the plate type is adopted in many fields because of its small size and high heat exchange efficiency. As a conventional plate heat exchanger, for example, a large number of corrugated plates are arranged at predetermined intervals, and a liquid such as a liquid and another liquid or gas to be heat-exchanged therewith are alternately passed between the corrugated plates. There is something.

【0003】[0003]

【発明が解決しようとする課題】しかし上記のような形
式の熱交換器では、その伝熱面全体に液を接触させるた
めに波形プレート間に常に一定容量の液体を滞留させ、
その滞留液の一部が供給される液体と入れ代わるように
している。そのため波形プレート間の液体量あたりの伝
熱面積は必然的に小さくなり、伝熱効率が低いという問
題があった。しかも比較的多い液体を貯留することによ
り水頭圧も増大するので、より確実な液漏れ対策を必要
とし、その結果装置が大きくなり重量も増大するという
問題があった。そこで本発明はこのような従来の問題を
解決する波形伝熱ユニット、およびその波形伝熱ユニッ
トにより構成される熱交換器を提供することを課題とす
るものである。
However, in a heat exchanger of the type described above, a constant volume of liquid is always retained between the corrugated plates in order to bring the liquid into contact with the entire heat transfer surface.
A part of the retained liquid is replaced with the supplied liquid. Therefore, there is a problem that the heat transfer area per liquid amount between the corrugated plates is necessarily small, and the heat transfer efficiency is low. In addition, since a relatively large amount of liquid is stored, the water head pressure also increases, so that more reliable measures against liquid leakage are required, and as a result, there is a problem that the apparatus becomes large and the weight increases. Therefore, an object of the present invention is to provide a waveform heat transfer unit that solves such a conventional problem, and a heat exchanger including the waveform heat transfer unit.

【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
の請求項1に記載の発明は、並行する一対の波形プレー
トがその間に導入される液体を毛細管作用により拡散さ
せるような間隔で互いに接合されていることを特徴とす
る熱交換器用の波形伝熱ユニットである。上記波形伝熱
ユニットによれば、一対の波形プレートの間隔が導入さ
れる液体を毛細管作用により拡散させるような極めて小
さな値とされる。そのためその間に滞留する液体量も少
ないために、該液体量あたりの伝熱面積が著しく大きく
なるので伝熱効率を高くすることができる。また波形伝
熱ユニット内に導入される液体はその毛細管作用により
伝熱面の隅々まで拡散し層流となって通過すると共に、
上記のように内部に滞留する液体量が極端に少ないこと
から水頭圧も低くなる。そのため液漏れ対策の問題が軽
減され、熱交換器を構成する際のシール構造が簡単にな
る。
According to the first aspect of the present invention, a pair of parallel corrugated plates are joined to each other at an interval such that a liquid introduced therebetween is diffused by capillary action. This is a wave heat transfer unit for a heat exchanger. According to the corrugated heat transfer unit, the interval between the pair of corrugated plates has an extremely small value such that the introduced liquid is diffused by capillary action. Therefore, since the amount of liquid staying in the meantime is also small, the heat transfer area per the amount of liquid is significantly increased, so that the heat transfer efficiency can be increased. In addition, the liquid introduced into the corrugated heat transfer unit diffuses to every corner of the heat transfer surface due to the capillary action and passes as a laminar flow,
As described above, since the amount of liquid staying inside is extremely small, the water head pressure also decreases. Therefore, the problem of liquid leakage countermeasures is reduced, and the seal structure when configuring the heat exchanger is simplified.

【0005】請求項2に記載の発明は、請求項1に記載
の発明の実施の形態であって、波形伝熱ユニットにおけ
る一方の端部に液体流入部が設けられ、他方の端部に液
体流出部が設けられていることを特徴とするものであ
る。このような波形伝熱ユニットを使用すると、熱交換
器をより簡単に組み立てることができる。請求項3に記
載の発明は、請求項2に記載の発明における好ましい実
施の形態であって、波形伝熱ユニットの上側に液体流入
部を位置させた縦型形式としたことを特徴とするもので
ある。このような縦型の波形伝熱ユニットでは、液体を
上側から導入して下側から排出するので、液体が毛細管
作用と自重作用でよりスムーズに波形伝熱ユニット内を
拡散し通過することができる。そのため水頭圧もより一
層低くなるのでシール構造もより簡単でよくなるという
利点がある。請求項4に記載の発明は、請求項2または
請求項3に記載の波形伝熱ユニットを複数整列して構成
される熱交換器であって、各波形伝熱ユニット内に液体
を通過させ、各波形伝熱ユニット間に該液体と熱交換す
べき流体を通過させるように構成されていることを特徴
とするものである。上記熱交換器は伝熱効率が高く、コ
ンパクトで且つ軽量に構成される。
The invention according to claim 2 is an embodiment of the invention according to claim 1, wherein a liquid inflow portion is provided at one end of the corrugated heat transfer unit and a liquid inflow portion is provided at the other end. An outflow portion is provided. The use of such a corrugated heat transfer unit makes it easier to assemble the heat exchanger. A third aspect of the present invention is a preferred embodiment of the second aspect of the present invention, characterized in that a vertical type in which a liquid inflow portion is located above a corrugated heat transfer unit. It is. In such a vertical waveform heat transfer unit, the liquid is introduced from the upper side and discharged from the lower side, so that the liquid can diffuse and pass through the waveform heat transfer unit more smoothly by the capillary action and the self-weight action. . Therefore, there is an advantage that the head structure is further reduced and the sealing structure is simpler and better. The invention according to claim 4 is a heat exchanger configured by arranging a plurality of the waveform heat transfer units according to claim 2 or 3, wherein a liquid is passed through each waveform heat transfer unit, It is characterized in that a fluid to be heat-exchanged with the liquid is passed between the corrugated heat transfer units. The heat exchanger has a high heat transfer efficiency, is compact and lightweight.

【0006】[0006]

【発明の実施の形態】次に、本発明の実施の形態を図面
に基づいて説明する。図1は本発明の波形伝熱ユニット
を縦型として多数並列して整列させた熱交換器の1例を
示す正面図、図2はそのII−II断面図、図3は図2にお
けるA部拡大図、図4は図3における波形プレートの部
分をさらに拡大した部分断面図である。これらの図にお
いて、各波形伝熱ユニット1はそれぞれ並列に配置され
た一対の波形プレート2を有している。波形プレート2
はアルミニウム、黄銅、ステンレスなどの伝熱性のよい
金属の波板から作られ、その周縁部を相互にろう付けす
ることにより密閉容器を形成している。そして波形伝熱
ユニット1の上端部と下端部には液体流入部3と液体流
出部4がそれぞれ設けられる。なお、波形プレート2の
表面には耐海水性、あるいは耐薬品性の樹脂皮膜を被着
してもよい。一対の波形プレート2の間隔は、上述のよ
うに導入される液体が毛細管作用により伝熱面の隅々ま
で拡散するような極めて狭い値であるが、通常0.1m
m〜1.0mm程度とされる。
Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a front view showing an example of a heat exchanger in which a large number of wave-shaped heat transfer units of the present invention are arranged in parallel in a vertical type, FIG. 2 is a cross-sectional view taken along the line II-II, and FIG. FIG. 4 is an enlarged view of a portion of the corrugated plate in FIG. In these figures, each of the wave heat transfer units 1 has a pair of wave plates 2 arranged in parallel. Corrugated plate 2
Is made of a corrugated sheet of a metal having good heat conductivity such as aluminum, brass, stainless steel, etc., and forms a hermetically sealed container by brazing the peripheral portions thereof to each other. A liquid inflow portion 3 and a liquid outflow portion 4 are provided at the upper end and the lower end of the waveform heat transfer unit 1, respectively. The surface of the corrugated plate 2 may be coated with a seawater-resistant or chemical-resistant resin film. The interval between the pair of corrugated plates 2 is an extremely narrow value such that the liquid introduced as described above diffuses to every corner of the heat transfer surface by capillary action, but is usually 0.1 m.
m to about 1.0 mm.

【0007】図3に示すように、液体流入部3は波形プ
レート2と同様な材料から作られるパイプ状のヘッダ−
3aと、そのヘッダ−3aと波形伝熱ユニット1内を連
通する連通部3bからなり、図1の矢印Bのようにヘッ
ダ−3aに供給される液体20は連通部3bを経て波形
伝熱ユニット1内に導入される。液体流出部4も液体流
入部3と同様なパイプ状のヘッダ−4aと、そのヘッダ
−4aと波形伝熱ユニット1内を連通する連通部4bか
らなり、波形伝熱ユニット1より流出する液体は連通部
4bを経てヘッダ−4aに入り図1の矢印Cのように排
出される。
As shown in FIG. 3, the liquid inflow section 3 has a pipe-shaped header made of the same material as the corrugated plate 2.
The liquid 20 supplied to the header 3a through the communication portion 3b as shown by the arrow B in FIG. 1 is composed of a communication portion 3b that communicates the header 3a with the inside of the waveform heat transfer unit 1. 1 is introduced. The liquid outflow portion 4 also includes a pipe-shaped header 4a similar to the liquid inflow portion 3, and a communication portion 4b that communicates the header 4a with the inside of the waveform heat transfer unit 1, and the liquid flowing out of the waveform heat transfer unit 1 The header 4a enters the header 4a via the communication portion 4b and is discharged as shown by an arrow C in FIG.

【0008】この例では、ヘッダ−3aおよびヘッダ−
4aが各波形伝熱ユニット1間のスペーサーとしても機
能しており、それによって形成される各波形の空間5に
液体20と熱交換する他の液体や気体などの流体21が
図1の二点鎖線のように通過する。なお空間5の出入口
以外の周縁部は、例えば図3のようにヘッダ−3a(ま
たはヘッダ−4a)の周囲にプラスチック製のシール剤
6を充填することによってシールされる。そして液体流
入部3から波形伝熱ユニット1内に導入された液体20
は、極めて狭い間隔の間を毛細管作用により拡散しなが
ら図1の実線のように上方から下方へ流下する間に横方
向に流れる流体21とその伝熱面を介して熱交換されて
液体流出部4より流出する。
In this example, header-3a and header-
4a also functions as a spacer between the wave-shaped heat transfer units 1, and a fluid 21 such as another liquid or gas that exchanges heat with the liquid 20 is formed in each wave-shaped space 5 formed by the two points in FIG. Pass like a dashed line. The periphery of the space 5 other than the entrance is sealed by filling a plastic sealing agent 6 around the header-3a (or the header-4a) as shown in FIG. 3, for example. Then, the liquid 20 introduced into the waveform heat transfer unit 1 from the liquid inflow section 3
The heat is exchanged with the fluid 21 flowing laterally while flowing down from the upper side to the lower side as shown by the solid line in FIG. It flows out from 4.

【0009】図5は図1に示した波形伝熱ユニット1を
複数組み込んだ空冷式の熱交換器の1例である。熱交換
器7の本体8の中央部には複数の波形伝熱ユニット1が
組み込まれ、液体20は供給部9から液体流入部3を経
て波形伝熱ユニット1内に流入され、液体流出部4を経
て排出部10より排出される。一方、本体8における波
形伝熱ユニット1の両側には気体導入部11と気体排出
部12が設けられ、さらに気体導入部11の外側にファ
ン13が取り付けられる。そして液体20と熱交換すべ
き外部空気などの流体21は、ファン13により気体導
入部11に導入され、波形伝熱ユニット1の空間5を経
て気体排出部12より排出される。
FIG. 5 shows an example of an air-cooled heat exchanger incorporating a plurality of the corrugated heat transfer units 1 shown in FIG. A plurality of corrugated heat transfer units 1 are incorporated in the center of the main body 8 of the heat exchanger 7, and the liquid 20 flows into the corrugated heat transfer unit 1 from the supply unit 9 via the liquid inflow unit 3, and the liquid outflow unit 4 Is discharged from the discharge unit 10 through On the other hand, a gas inlet 11 and a gas outlet 12 are provided on both sides of the waveform heat transfer unit 1 in the main body 8, and a fan 13 is mounted outside the gas inlet 11. Then, a fluid 21 such as external air to be heat-exchanged with the liquid 20 is introduced into the gas introduction unit 11 by the fan 13 and discharged from the gas discharge unit 12 through the space 5 of the waveform heat transfer unit 1.

【0010】[0010]

【発明の効果】以上のように、請求項1に記載の波形伝
熱ユニットは、並行する一対の波形プレートがその間に
導入される液体を毛細管作用により拡散させるような間
隔で互いに接合されているので、波形プレート内に滞留
する液体量が極めて少なくなる。そのため該液体量あた
りの伝熱面積が著しく大きくなり高い伝熱効率が得られ
る。また波形伝熱ユニット内に導入される液体は、その
毛細管作用により伝熱面の隅々まで拡散し層流となって
通過し、上記のように内部に滞留する液体量も極端に少
ないことから水頭圧も低くなる。そのため液漏れ対策の
問題が軽減され熱交換器を構成する際のシール構造が簡
単になる。
As described above, in the corrugated heat transfer unit according to the first aspect, a pair of parallel corrugated plates are joined to each other at an interval such that the liquid introduced therebetween is diffused by capillary action. Therefore, the amount of liquid staying in the corrugated plate is extremely small. Therefore, the heat transfer area per liquid amount is significantly increased, and high heat transfer efficiency is obtained. Also, the liquid introduced into the corrugated heat transfer unit is diffused to every corner of the heat transfer surface due to its capillary action, passes as a laminar flow, and the amount of liquid staying inside as described above is extremely small. The head pressure also decreases. Therefore, the problem of liquid leakage countermeasures is reduced, and the seal structure when configuring the heat exchanger is simplified.

【0011】請求項2に記載の波形伝熱ユニットは、波
形伝熱ユニットにおける一方の端部に液体流入部が設け
られ、他方の端部に液体流出部が設けられているので、
熱交換器をより簡単に組み立てることができる。請求項
3に記載の波形伝熱ユニットは、波形伝熱ユニットの上
側に液体流入部を位置させた縦型形式としたことを特徴
とする。このような縦型の波形伝熱ユニットでは、液体
を上側から導入して下側から排出するので、液体が毛細
管作用と自重作用でよりスムーズに波形伝熱ユニット内
を拡散し通過することができる。そのため水頭圧もより
一層低くなるのでシール構造もより簡単でよい。請求項
4に記載の熱交換器は、各波形伝熱ユニット内に液体を
通過させ、各波形伝熱ユニット間に該液体と熱交換すべ
き流体を通過させるように構成されているので、伝熱効
率が高く、コンパクトで且つ軽量になる。
According to the second aspect of the present invention, the liquid heat transfer unit has a liquid inflow portion at one end and a liquid outflow portion at the other end.
The heat exchanger can be more easily assembled. According to a third aspect of the present invention, the waveform heat transfer unit is of a vertical type in which the liquid inflow portion is located above the waveform heat transfer unit. In such a vertical waveform heat transfer unit, the liquid is introduced from the upper side and discharged from the lower side, so that the liquid can diffuse and pass through the waveform heat transfer unit more smoothly by the capillary action and the self-weight action. . As a result, the head pressure is further reduced, so that the sealing structure may be simpler. Since the heat exchanger according to claim 4 is configured to pass the liquid through each wave-shaped heat transfer unit and to pass the fluid to be heat-exchanged with the liquid between each wave-shaped heat transfer unit, High thermal efficiency, compact and lightweight.

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

【図1】本発明の波形伝熱ユニットを縦型として多数並
列して整列させた熱交換器の1例を示す正面図。
FIG. 1 is a front view showing an example of a heat exchanger in which a large number of waveform heat transfer units of the present invention are arranged in parallel in a vertical type.

【図2】図1のII−II断面図。FIG. 2 is a sectional view taken along line II-II of FIG.

【図3】図2におけるA部拡大図。FIG. 3 is an enlarged view of a portion A in FIG. 2;

【図4】図3における波形プレートの部分をさらに拡大
した部分断面図。
FIG. 4 is a partial cross-sectional view further enlarging a corrugated plate portion in FIG. 3;

【図5】図1の波形伝熱ユニットを使用する空冷式熱交
換器の1例を示す正面図。
FIG. 5 is a front view showing an example of an air-cooled heat exchanger using the waveform heat transfer unit of FIG. 1;

【符号の説明】[Explanation of symbols]

1 波形伝熱ユニット 2 波形プレート 3 液体流入部 3a ヘッダ− 3b 連通部 4 液体流出部 4a ヘッダ− 4b 連通部 5 空間 6 シール剤 7 熱交換器 8 本体 9 供給部 10 排出部 11 気体導入部 12 気体排出部 13 ファン 20 液体 21 流体 DESCRIPTION OF SYMBOLS 1 Corrugated heat transfer unit 2 Corrugated plate 3 Liquid inflow part 3a Header 3b communication part 4 Liquid outflow part 4a Header 4b communication part 5 Space 6 Sealant 7 Heat exchanger 8 Main body 9 Supply part 10 Discharge part 11 Gas introduction part 12 Gas discharge unit 13 Fan 20 Liquid 21 Fluid

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 並行する一対の波形プレート2がその間
に導入される液体20を毛細管作用により拡散させるよ
うな間隔で互いに接合されていることを特徴とする熱交
換器用の波形伝熱ユニット。
1. A corrugated heat transfer unit for a heat exchanger, wherein a pair of parallel corrugated plates 2 are joined to each other at intervals such that a liquid 20 introduced therebetween is diffused by capillary action.
【請求項2】 波形伝熱ユニットにおける一方の端部に
液体流入部3が設けられ、他方の端部に液体流出部4が
設けられている請求項1に記載の熱交換器用の波形伝熱
ユニット。
2. The waveform heat transfer for a heat exchanger according to claim 1, wherein a liquid inflow portion 3 is provided at one end of the waveform heat transfer unit, and a liquid outflow portion 4 is provided at the other end. unit.
【請求項3】 液体流入部3が上側に位置される縦型の
波形伝熱ユニットである請求項2に記載の熱交換器用の
波形伝熱ユニット。
3. The wave-shaped heat transfer unit for a heat exchanger according to claim 2, wherein the liquid inflow section 3 is a vertical wave-shaped heat transfer unit located on the upper side.
【請求項4】 請求項2または請求項3に記載の波形伝
熱ユニットが複数整列され、各波形伝熱ユニット内に液
体20が通過し各波形伝熱ユニット間に該液体と熱交換
すべき流体21が通過するようになされた熱交換器。
4. A plurality of corrugated heat transfer units according to claim 2 or 3, wherein a liquid 20 passes through each corrugated heat transfer unit, and heat exchange with the liquid is performed between each corrugated heat transfer unit. A heat exchanger adapted to pass through the fluid 21.
JP3217498A 1998-01-28 1998-01-28 Waveform heat transfer unit and heat exchanger Pending JPH11211367A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3217498A JPH11211367A (en) 1998-01-28 1998-01-28 Waveform heat transfer unit and heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3217498A JPH11211367A (en) 1998-01-28 1998-01-28 Waveform heat transfer unit and heat exchanger

Publications (1)

Publication Number Publication Date
JPH11211367A true JPH11211367A (en) 1999-08-06

Family

ID=12351582

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3217498A Pending JPH11211367A (en) 1998-01-28 1998-01-28 Waveform heat transfer unit and heat exchanger

Country Status (1)

Country Link
JP (1) JPH11211367A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4808732B2 (en) * 2004-12-22 2011-11-02 シユテイーベル・エルトロン・ゲゼルシヤフト・ミツト・ベシユレンクテル・ハフツング・ウント・コンパニー・コマンデイトゲゼルシヤフト Heat exchanger and heat pump circuit

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4808732B2 (en) * 2004-12-22 2011-11-02 シユテイーベル・エルトロン・ゲゼルシヤフト・ミツト・ベシユレンクテル・ハフツング・ウント・コンパニー・コマンデイトゲゼルシヤフト Heat exchanger and heat pump circuit

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