JPS62131196A - Heat exchanger of plate fin type - Google Patents

Heat exchanger of plate fin type

Info

Publication number
JPS62131196A
JPS62131196A JP27193185A JP27193185A JPS62131196A JP S62131196 A JPS62131196 A JP S62131196A JP 27193185 A JP27193185 A JP 27193185A JP 27193185 A JP27193185 A JP 27193185A JP S62131196 A JPS62131196 A JP S62131196A
Authority
JP
Japan
Prior art keywords
primary
sections
cylindrical
spaces
corrugated
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
JP27193185A
Other languages
Japanese (ja)
Inventor
Akihiko Ooyama
大山 昭彦
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.)
IHI Corp
Original Assignee
IHI 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 IHI Corp filed Critical IHI Corp
Priority to JP27193185A priority Critical patent/JPS62131196A/en
Publication of JPS62131196A publication Critical patent/JPS62131196A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To reduce the number of parts and provide simplification and light weight in the structure by providing in series cross flow sections and counter flow sections and providing corrugated boards in the cross flow sections, the directions of the corrugated boards being mutually different, alternately among partition boards and at four corners of the partition board piercing specified connecting sections. CONSTITUTION:Rectaugular partition boards 3a and 3b each with a flange section are alternately piled up in a plurality of steps, and respective fauges 2 are mutually joined to form primary spaces 8a and secondary spaces 8b. Between the partition boards 3a and 3b a corrugated board 7a forming a primary flow passage and a corrugated board 7b forming a secondary flow passage are alternately arranged and fixed. Further, the partition boards have respectively cylindrical sections 9a and 9b projected. Those cylindrical projections fit in an opening 1 which is located right below the cylindrical projection to be joined together, so that primary spaces 8a are mutually connected and so are secondary spaces 8b. Primary fluid I passes through each of cylindrical section 9a and it is led to the primary space 8a of each step, and secondary fluid II passes through each of cylindrical sections 9b and it is led to the secondary space 8b of each step, and beat exchange occurs between the primary and secondary flow passages. With this constitution a cussing which covers the whole structure, distance plate, spacer, etc. are not required, making it possible to reduce the number of parts and provide a light weight heat exchanger.

Description

【発明の詳細な説明】 [産業上の利用分野1 本発明は、紡カプラント、化学プラント等で、ガス−ガ
ス、液−液、或いはガス−液の間接熱交換器として使用
するプレートフィン型熱交換器に関するものである。
Detailed Description of the Invention [Industrial Application Field 1] The present invention is a plate-fin type heat exchanger used as a gas-gas, liquid-liquid, or gas-liquid indirect heat exchanger in spinning plants, chemical plants, etc. It concerns exchangers.

[従来の技術] 例えば、伝熱面を波板としたプレートフィン型熱交換器
のうちには、第5図に示す如く、交差流部aと対向流部
すをもつものがあり、交差流部aでは、高温流体を流す
流路Cと低温流体を流す流路dとが斜交し、対向流部す
では、流路Cと流路dとが平行に配した構成としである
[Prior Art] For example, among plate-fin type heat exchangers whose heat transfer surface is a corrugated plate, there is one that has a cross-flow section a and a counter-flow section A, as shown in Fig. 5. In the section a, the flow path C through which the high-temperature fluid flows and the flow path d through which the low-temperature fluid flows intersect obliquely, and in the opposing flow section, the flow path C and the flow path d are arranged in parallel.

[発明が解決しようとする問題点] 而して、斯かるプレートフィン型熱交換器においては、
流路c、dを形成するための波板e、fを上下方向に複
数段積層すると共に、波板e、f間には夫々隔壁板を介
在させる必要があり、その他ディスタンスプレートやス
ペーサー、伝熱促進用ねじり棒等の部品が数多く必要で
あり、更にはこれらの部品全体を収容するケーシングも
必要である。従って、構造が複雑で且つ重量的にも大と
なっていた。
[Problems to be solved by the invention] Therefore, in such a plate-fin type heat exchanger,
It is necessary to stack corrugated plates e and f in multiple stages vertically to form channels c and d, and to interpose partition plates between each of the corrugated plates e and f, as well as distance plates, spacers, and transmission plates. A large number of parts are required, such as heat-enhancing torsion rods, and a casing is also required to house all of these parts. Therefore, the structure is complicated and the weight is also large.

本発明はこのような実情に鑑み、部品点数を減少して構
造及び製作方法の簡素化、並びに軽量化を図ろうとする
ものである。
In view of these circumstances, the present invention aims to reduce the number of parts, simplify the structure and manufacturing method, and reduce the weight.

[問題点を解決するための手段] 本発明は、4隅に開口を穿設し周縁部にフランジ部を設
けた隔壁板を上下方向に複数段積層すると共に、交差流
部と対向流部を連設して成り且つ交差流部の向きが互い
に異なる波板を、前記隔壁板間に交互に配設し、更に前
記隔壁板の各段間相互では異なり一段置きでは同一対角
線上に位置する開口に円筒部を突設し、該円筒部を該円
筒部直下の開口に接続して成る構成を有する。
[Means for Solving the Problems] The present invention consists of vertically stacking a plurality of partition plates each having openings at the four corners and a flange at the peripheral edge, and a cross-flow section and a counter-flow section. Corrugated plates that are connected in series and have mutually different directions of cross-flow portions are arranged alternately between the partition plates, and further, openings that are different between each stage of the partition plates and are located on the same diagonal line every other stage. It has a configuration in which a cylindrical portion is provided protrudingly from the cylindrical portion and the cylindrical portion is connected to an opening directly below the cylindrical portion.

[作   用] 従って、複数段積層した隔壁板のフランジ部及び円筒部
によって、従来の如きディスタンスプレートやスペーサ
ー、ケーシング等の部品を兼ねることができる。
[Function] Therefore, the flange portion and cylindrical portion of the partition wall plates stacked in multiple stages can serve as conventional parts such as distance plates, spacers, and casings.

[実 施 例] 以下、図面を参照して本発明の詳細な説明する。[Example] Hereinafter, the present invention will be described in detail with reference to the drawings.

第1図乃至第3図に示す如く、4隅部に流体の連通部と
なる開口1を夫々穿設し、且つ外縁部にプレス加工によ
って所要角度で末広テーパー状に折曲げ加工したフラン
ジ部2を有する矩形の隔壁板3a、3bを、前記各フラ
ンジ部2が嵌合するよう上下方向に交互に複数段積層し
て各フランジ部2同士を接合し、隔壁板3a内に一次側
空間8aを隔壁板3b内に二次側空間8bを夫々形成す
る。又隔壁板3a、3b間には、即ち一次側空間8aと
二次側空間8bには、第4図(イ)に示す如く両端に交
差流部4aを又その中間に対向流部5aを備えた一次側
流路形成用波板7aと、第4図(0)に示す如く前記波
板7aの交差流部4aに対し斜交づる交差流部4bと対
向流部5aに対し平行な対向流部5bを備えた二次側流
路形成用波板1bとを、交互に配置固定する。更に、隔
壁板3aには一方の対角線上に位置する開口1部に、又
隔壁板3bには他方の対角線上に位置する開口1部に夫
々円筒部9a 、 9bを突設し、該各回筒部9a、9
bの下端を、その直下に位置する開口1に嵌合接合し、
−次側空間88同士及び二次側空間8b同士を連通させ
ると共に一次側空間8aと二次側空間8bとを遮断する
よう構成する。
As shown in FIGS. 1 to 3, a flange portion 2 has openings 1 formed at each of the four corners and serves as a fluid communication portion, and the outer edge portion is bent into a wide taper shape at a predetermined angle by press working. A plurality of rectangular partition plates 3a and 3b having the following shapes are stacked alternately in the vertical direction so that the respective flange parts 2 fit together, and the flange parts 2 are joined together, thereby creating a primary space 8a in the partition plate 3a. Secondary spaces 8b are respectively formed within the partition plates 3b. Further, between the partition plates 3a and 3b, that is, the primary space 8a and the secondary space 8b, as shown in FIG. As shown in FIG. 4(0), the corrugated plate 7a for forming a primary flow path has a cross flow part 4b obliquely intersecting with the cross flow part 4a of the corrugated plate 7a, and a counter flow parallel to the counter flow part 5a. The corrugated plates 1b for forming a secondary flow path having portions 5b are arranged and fixed alternately. Furthermore, cylindrical portions 9a and 9b are provided protruding from one opening located on one diagonal of the partition plate 3a, and cylindrical portions 9b are provided protruding from one opening located on the other diagonal of the partition plate 3b, respectively. Part 9a, 9
The lower end of b is fitted and joined to the opening 1 located directly below it,
- The primary space 8a and the secondary space 8b are configured to be communicated with each other and the primary space 88 and the secondary space 8b.

又、最上段に位置する隔壁板3aの各開口1には、例え
ば第1図の右上の開口1に一次側流体供給ヘッダー10
aを、又左下の開口1に一次側流体排出ヘッダー11a
を夫々取付け、一方左上の開口1に二次側流体供給ヘッ
ダー10bを、又右下の開口1に二次側流体排出ヘッダ
ー11bを夫々取付ける。尚、最下段に位置する隔壁板
3aの各開口1部には、ノズル6を夫々設けると共に、
該ノズル6部に図示しない流体温度計測器を設置して、
夫々−次側、二次側で給排する流体の温度を計測し得る
ようにしたり、或いは閉塞キャップ等を取付ける。
Further, each opening 1 of the partition wall plate 3a located at the uppermost stage is provided with a primary fluid supply header 10, for example, at the upper right opening 1 in FIG.
a, and the primary side fluid discharge header 11a to the lower left opening 1.
On the other hand, the secondary side fluid supply header 10b is installed in the upper left opening 1, and the secondary side fluid discharge header 11b is installed in the lower right opening 1. In addition, a nozzle 6 is provided in each opening of the partition wall plate 3a located at the lowest stage, and
A fluid temperature measuring device (not shown) is installed in the nozzle 6,
It is possible to measure the temperature of the fluid being supplied and discharged on the downstream and secondary sides, respectively, or a closing cap or the like is installed.

斯かる構成としであるので、−次側供給ヘッダ−10a
から供給された一次流体工は、最上段では直接、又それ
より下段では夫々円筒部9bを通って各段の一次側空間
8aに導かれ、−次側流路を形成する波板1aの交差流
部4a、対向流部5a、交差流部4aを通り一次側排出
ヘッダー11aより排出され、一方、二次側供給ヘッダ
ー10bから供給された二次流体■は、夫々円筒部9b
を過つて各段の二次側空間8bに導かれ、二次側流路を
形成する波板1bの交差流部4b、対向流部5b、交差
流部4bを通り二次側排出ヘッダー11bより排出され
、而して、流体1.I[は−次側と二次側の流路間で熱
交換される。
With such a configuration, the -next side supply header 10a
The primary fluid supplied from the uppermost stage is directly guided to the primary space 8a of each stage, and the lower stage is led to the primary space 8a of each stage through the cylindrical part 9b. The secondary fluid ■ is discharged from the primary discharge header 11a through the flow section 4a, the counterflow section 5a, and the cross flow section 4a, while the secondary fluid ■ supplied from the secondary supply header 10b is discharged from the cylindrical section 9b, respectively.
is led to the secondary side space 8b of each stage, passes through the cross flow part 4b, the counter flow part 5b, and the cross flow part 4b of the corrugated plate 1b forming the secondary flow path from the secondary side discharge header 11b. The fluid 1. I[ is heat exchanged between the downstream and secondary flow paths.

前記において、隔壁板3a、3bは円筒部9a、9bと
フランジ部2をもつだけであるため構造が極めて簡単で
あり、7ランジ部2の接合によって側壁が構成されるの
で、全体を覆うケーシングが不要となり、更に円筒部9
a、9bとその直下の開口1を接合することによって、
−次側空間8aと二次側空間8bの形成保持及び−次側
空間8aと二次側空間8bのシールが行われるため、従
来の如きディスタンスプレートやスペーサーが不要であ
り、著しく部品点数を減することができ、軽量化が図ら
れる。
In the above, the partition plates 3a and 3b have only the cylindrical parts 9a and 9b and the flange part 2, so the structure is extremely simple, and the side wall is formed by joining the seven flange parts 2, so the casing that covers the whole is No longer needed, and the cylindrical part 9
By joining a, 9b and the opening 1 directly below,
- Since the formation and maintenance of the downstream space 8a and the secondary side space 8b and the sealing of the downstream space 8a and the secondary side space 8b are performed, there is no need for conventional distance plates or spacers, and the number of parts can be significantly reduced. The weight can be reduced.

尚、本発明は前記実施例にのみ限定されるものではなく
、波板の流路部にねじり板を配して伝熱促進を図ること
等は任意であり、その伯本発明の要旨を逸脱しない限り
種々変更を加え得ることは勿論である。
It should be noted that the present invention is not limited to the above-mentioned embodiments, and it is optional to arrange a twisted plate in the flow path section of the corrugated plate to promote heat transfer, and this departs from the gist of the present invention. Of course, various changes can be made as long as it is not necessary.

[発明の効果] 以上説明したように本発明のプレートフィン型熱交換器
によれば、部品点数が少ないので、小型化、軽量化並び
に製作の容易化を図り得る、と言う優れた効果を秦し得
る。
[Effects of the Invention] As explained above, the plate-fin type heat exchanger of the present invention has the excellent effects of being smaller, lighter, and easier to manufacture because the number of parts is small. It is possible.

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

第1図は本発明のプレートフィン型熱交換器の平面図、
第2図は第1図の■−■矢視図、第3図は第1図の■−
■矢視図、第4図(イ)(ロ)は波板の説明図、第5図
は従来のプレートフィン型熱交換器の説明図である。 1は開口、2はフランジ、3a、3bは隔壁板、4a、
4bは交差流部、5a、5bは対向流部、7a、7bは
波板、8aは一次側空間、8bは二次側空間、9a。 9bは円筒部を示す。
FIG. 1 is a plan view of the plate-fin type heat exchanger of the present invention;
Figure 2 is a view from the ■-■ arrow in Figure 1, and Figure 3 is a view from ■-■ in Figure 1.
(2) A view in the direction of the arrows, FIGS. 4(A) and 4(B) are explanatory views of a corrugated plate, and FIG. 5 is an explanatory view of a conventional plate-fin type heat exchanger. 1 is an opening, 2 is a flange, 3a, 3b are partition plates, 4a,
4b is a cross-flow section, 5a and 5b are counter-flow sections, 7a and 7b are corrugated plates, 8a is a primary space, 8b is a secondary space, and 9a. 9b indicates a cylindrical portion.

Claims (1)

【特許請求の範囲】[Claims] 1)4隅に開口を穿設し周縁部にフランジ部を設けた隔
壁板を上下方向に複数段積層すると共に、交差流部と対
向流部を連設して成り且つ交差流部の向きが互いに異な
る波板を、前記隔壁板間に交互に配設し、更に前記隔壁
板の各段間相互では異なり一段置きでは同一対角線上に
位置する開口に円筒部を突設し、該円筒部を該円筒部直
下の開口に接続して成ることを特徴とするプレートフィ
ン型熱交換器。
1) A plurality of partition plates with openings in the four corners and flanges on the periphery are stacked in multiple stages in the vertical direction, and a cross-flow part and a counter-flow part are connected in series, and the direction of the cross-flow part is Different corrugated plates are arranged alternately between the partition plates, and further, cylindrical parts are provided protruding from openings located on the same diagonal line at every other stage, which are different between each stage of the partition plates, and the cylindrical parts are A plate-fin type heat exchanger, characterized in that it is connected to an opening directly below the cylindrical portion.
JP27193185A 1985-12-03 1985-12-03 Heat exchanger of plate fin type Pending JPS62131196A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27193185A JPS62131196A (en) 1985-12-03 1985-12-03 Heat exchanger of plate fin type

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27193185A JPS62131196A (en) 1985-12-03 1985-12-03 Heat exchanger of plate fin type

Publications (1)

Publication Number Publication Date
JPS62131196A true JPS62131196A (en) 1987-06-13

Family

ID=17506842

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27193185A Pending JPS62131196A (en) 1985-12-03 1985-12-03 Heat exchanger of plate fin type

Country Status (1)

Country Link
JP (1) JPS62131196A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU707014B2 (en) * 1995-10-23 1999-07-01 Swep International Ab A plate heat exchanger
US6247528B1 (en) 1997-06-25 2001-06-19 Alfa Laval Ab Plate heat exchanger
WO2014132602A1 (en) * 2013-02-27 2014-09-04 株式会社デンソー Stacked heat exchanger
JP2014163639A (en) * 2013-02-27 2014-09-08 Denso Corp Lamination type heat exchanger

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU707014B2 (en) * 1995-10-23 1999-07-01 Swep International Ab A plate heat exchanger
US6247528B1 (en) 1997-06-25 2001-06-19 Alfa Laval Ab Plate heat exchanger
WO2014132602A1 (en) * 2013-02-27 2014-09-04 株式会社デンソー Stacked heat exchanger
JP2014163639A (en) * 2013-02-27 2014-09-08 Denso Corp Lamination type heat exchanger
US10962307B2 (en) 2013-02-27 2021-03-30 Denso Corporation Stacked heat exchanger

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