JPH0684176U - Plate fin type heat exchanger - Google Patents
Plate fin type heat exchangerInfo
- Publication number
- JPH0684176U JPH0684176U JP2463293U JP2463293U JPH0684176U JP H0684176 U JPH0684176 U JP H0684176U JP 2463293 U JP2463293 U JP 2463293U JP 2463293 U JP2463293 U JP 2463293U JP H0684176 U JPH0684176 U JP H0684176U
- Authority
- JP
- Japan
- Prior art keywords
- plate
- heat exchanger
- pressure
- type heat
- plates
- 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
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
(57)【要約】
【目的】 通路を構成するプレートの最適化を図り、小
型軽量化を図ったプレートフィン型熱交換器の提供。
【構成】 流体圧力が異なる2流体の熱交換を行うもの
で、高圧流体通路1にはその流体圧力に応じて板厚を選
定した厚肉プレート2,2並びに狭ピッチフィン3を用
い、他の低圧流体通路4には薄肉プレート5並びに広ピ
ッチフィン6を用い、所要部にサイドバー7を配置して
これらを積層し、一体にろう付け組み立てしてある。
【効果】 積層寸法並びに重量を低減することができ、
特に、プレート材質がアルミニウムまたはステンレス鋼
あるいは流体に応じて両材料を組み合わせた場合に顕著
な小型軽量化の効果が得られる。
(57) [Summary] [Purpose] To provide a plate fin type heat exchanger that is compact and lightweight by optimizing the plates that form the passages. [Structure] Heat exchange between two fluids having different fluid pressures is performed. In the high-pressure fluid passage 1, thick plates 2 and 2 having a thickness selected according to the fluid pressure and a narrow pitch fin 3 are used. A thin plate 5 and a wide pitch fin 6 are used for the low-pressure fluid passage 4, a side bar 7 is arranged at a required portion, these are laminated, and integrally brazed and assembled. [Effect] Stacking size and weight can be reduced,
In particular, when the plate material is aluminum or stainless steel, or when both materials are combined depending on the fluid, a remarkable size and weight reduction effect can be obtained.
Description
【0001】[0001]
この考案は、プレートフィン型熱交換器の改良に係り、通路の流体圧力に応じ てプレート板厚を選定し、小型軽量化を図ったプレートフィン型熱交換器に関す る。 The present invention relates to an improvement of a plate fin type heat exchanger, and relates to a plate fin type heat exchanger in which the plate thickness is selected according to the fluid pressure in a passage to reduce the size and weight.
【0002】[0002]
プレートフィン型熱交換器は、例えば、波形フィンとプレートを交互に所要数 を積層し、プレート間の所要端部にサイドバーを介在させて、ろう付けで一体化 し、プレート間にフィンを挟み周囲をサイドバーにて閉塞した通路を多数積層し た構成からなる。 小型で熱交換効率がすぐれていることから、多方面の用途の熱交換器に利用さ れている。 In the plate fin type heat exchanger, for example, a required number of corrugated fins and plates are alternately laminated, a side bar is interposed at a required end between the plates, and they are integrated by brazing, and the fins are sandwiched between the plates. It consists of a number of stacked passages that are closed by side bars. Due to its small size and excellent heat exchange efficiency, it is used in heat exchangers for various purposes.
【0003】[0003]
従来、プレートフィン型熱交換器では熱交換させる複数流体のうち、最も高い 流体圧力に耐えるようプレートの板厚を選定し、積層するプレートの全てにこの 高圧流体用の板厚の厚いプレートを用いて組み立てていた。 従って、高圧流体通路数が全通路数に対して少ない場合でも、全て板厚の厚い プレートを用いるため、積層寸法が大きくかつ重くなる。 Conventionally, in plate fin type heat exchangers, the plate thickness of the plates is selected to withstand the highest fluid pressure of the multiple fluids to be heat-exchanged, and the thick plates for this high-pressure fluid are used for all the laminated plates. I was assembling it. Therefore, even if the number of high-pressure fluid passages is small relative to the total number of passages, since thick plates are all used, the stacking dimension is large and heavy.
【0004】 この考案は、熱交換させる複数流体の流体圧力が異なるプレートフィン型熱交 換器において、通路を構成するプレートの最適化を図り、小型軽量化を図ったプ レートフィン型熱交換器の提供を目的としている。The present invention is a plate fin type heat exchanger in which a plurality of fluids to be heat-exchanged have different fluid pressures, and the plates forming the passages are optimized to reduce the size and weight of the plate fin type heat exchanger. The purpose is to provide.
【0005】[0005]
この考案は、プレート間にフィンを挟み周囲をサイドバーにて閉塞した通路を 複数積層したプレートフィン型熱交換器において、当該通路の流体圧力及び隣接 通路の流体圧力に応じてプレート板厚を選定し、板厚の異なるプレートを同一熱 交換器内に用いたことを特徴とするプレートフィン型熱交換器である。 This invention is a plate fin type heat exchanger in which multiple fins are sandwiched between plates and closed by side bars, and the plate thickness is selected according to the fluid pressure of the passage and the fluid pressure of the adjacent passage. However, the plate fin type heat exchanger is characterized in that plates having different plate thicknesses are used in the same heat exchanger.
【0006】[0006]
この考案は、熱交換させる複数流体の流体圧力が異なる場合、高圧流体通路の みに板厚の厚いプレートを用いて、さらにその他の通路の流体圧力に応じて選定 された板厚のプレートを用いることを特徴とし、例えば、3流体とも流体圧力が 異なる場合は、その圧力に応じて2種類または3種類の板厚みのプレートをそれ ぞれ当該流体通路位置に配置して積層するもので、最も高圧流体用の板厚の厚い プレートを全ての通路形成に用いる場合に比べて、通路を構成するプレート厚み の最適化を図ることができ、積層寸法並びに重量を低減することができる。 This invention uses a thick plate only for the high-pressure fluid passage and a plate with a thickness selected according to the fluid pressure of other passages when the fluid pressures of the multiple fluids to be heat-exchanged differ. For example, when the fluid pressures of the three fluids are different, two or three types of plates having different plate thicknesses are arranged at the fluid passage positions and laminated according to the pressures. As compared with the case where a thick plate for high-pressure fluid is used for forming all the passages, the thickness of the plates forming the passages can be optimized, and the stacking dimension and weight can be reduced.
【0007】[0007]
実施例1 図1に示すプレートフィン型熱交換器は、流体圧力が異なる2流体の熱交換を 行うもので、高圧流体通路1にはその流体圧力に応じて板厚を選定した厚肉プレ ート2,2並びに狭ピッチフィン3を用い、他の低圧流体通路4には薄肉プレー ト5並びに広ピッチフィン6を用い、所要部にサイドバー7を配置してこれらを 積層し、一体にろう付け組み立てしてある。 図示のごとく低圧、高圧、低圧、低圧、高圧、低圧、低圧、高圧、低圧の順に 積層されることになり、従来では10枚のプレート全てが厚肉プレートとなるが 、この考案では6枚のみ厚肉プレートを用いればよく、例えば、高圧流体通路1 の設計圧力50kg/cm2gでプレート板厚1.6mm、低圧流体通路4の設 計圧力5kg/cm2gでプレート板厚1mmとすれば、積層高さが2.4mm 、重量が2.4mm厚みのプレート1枚分、それぞれ軽減されることになる。Example 1 The plate fin type heat exchanger shown in FIG. 1 performs heat exchange between two fluids having different fluid pressures. The high pressure fluid passage 1 has a thick wall plate whose plate thickness is selected according to the fluid pressure. 2 and the narrow pitch fin 3 are used, the thin plate 5 and the wide pitch fin 6 are used for the other low-pressure fluid passages 4, and the side bar 7 is arranged at a required portion and these are laminated to be integrated. It is assembled and attached. As shown, low pressure, high pressure, low pressure, low pressure, high pressure, low pressure, low pressure, high pressure, and low pressure are laminated in this order. Conventionally, all 10 plates are thick plates, but only 6 plates in this invention. A thick plate may be used. For example, the plate pressure is 1.6 mm when the design pressure of the high pressure fluid passage 1 is 50 kg / cm 2 g and the plate pressure is 1 mm when the design pressure of the low pressure fluid passage 4 is 5 kg / cm 2 g. In this case, the stacking height is 2.4 mm and the weight is 2.4 mm, which is reduced by one plate.
【0008】 実施例2 さらに、4通路に流体圧力が異なる3流体の熱交換を行うプレートフィン型熱 交換器をアルミニウム材で組み立てる場合、積層順にA〜D通路とすると、 A通路 設計圧力20kg/cm2g プレート板厚1.2mm(a) B通路 設計圧力5kg/cm2g プレート板厚1mm(b) C通路 設計圧力5kg/cm2g プレート板厚1mm(b) D通路 設計圧力50kg/cm2g プレート板厚1.6mm(c) なる設計において、プレート板厚は積層順に、a,a,b,c,cとなり、全て cを使用する従来に比べて積層高さが1.4mm、重量が1.4mm厚みのプレ ート1枚分、それぞれ軽減され、A〜D通路を1単位として複数単位積層する熱 交換器の場合は、さらに積層高さと重量が軽減されることになる。Example 2 Further, when assembling a plate fin type heat exchanger for exchanging heat of three fluids having different fluid pressures in four passages from an aluminum material, if the passages A to D are arranged in the stacking order, A passage design pressure 20 kg / cm 2 g Plate thickness 1.2 mm (a) B passage Design pressure 5 kg / cm 2 g Plate thickness 1 mm (b) C passage Design pressure 5 kg / cm 2 g Plate thickness 1 mm (b) D passage Design pressure 50 kg / cm 2 g Plate plate thickness 1.6 mm (c) In the design, the plate thickness is a, a, b, c, c in the stacking order, and the stacking height is 1.4 mm compared to the conventional case where c is used. , The weight is reduced by one plate having a thickness of 1.4 mm, and in the case of a heat exchanger in which a plurality of units are stacked with A to D passages as one unit, the stacking height and weight should be further reduced. become.
【0009】[0009]
この考案は、実施例に示すごとく、流体圧力が異なる複数流体の熱交換を行う プレートフィン型熱交換器において、通路を構成するプレート厚みの最適化を図 ることができ、積層寸法並びに重量を低減することができ、特に、プレート材質 がアルミニウムまたはステンレス鋼あるいは流体に応じて両材料を組み合わせた 場合に顕著な小型軽量化の効果が得られる。 This invention, as shown in the embodiment, can optimize the thickness of the plates forming the passages in a plate fin type heat exchanger that performs heat exchange of a plurality of fluids having different fluid pressures, and can reduce the stacking dimension and weight. It can be reduced, and in particular, when the plate material is aluminum or stainless steel, or when both materials are combined depending on the fluid, a remarkable size and weight reduction effect can be obtained.
【図1】この考案によるプレートフィン型熱交換器の構
成を示す縦断説明図である。FIG. 1 is a vertical cross-sectional explanatory view showing a configuration of a plate fin type heat exchanger according to the present invention.
1 高圧流体通路 2 厚肉プレート 3 狭ピッチフィン 4 低圧流体通路 5 薄肉プレート 6 広ピッチフィン 7 サイドバー 1 High Pressure Fluid Passage 2 Thick Wall Plate 3 Narrow Pitch Fin 4 Low Pressure Fluid Passage 5 Thin Plate 6 Wide Pitch Fin 7 Sidebar
Claims (1)
バーにて閉塞した通路を複数積層したプレートフィン型
熱交換器において、当該通路の流体圧力及び隣接通路の
流体圧力に応じてプレート板厚を選定し、板厚の異なる
プレートを同一熱交換器内に用いたことを特徴とするプ
レートフィン型熱交換器。1. A plate fin type heat exchanger in which a plurality of passages having fins sandwiched between plates and the periphery of which is closed by a side bar are laminated, and the plate thickness is changed according to the fluid pressure of the passages and the fluid pressure of the adjacent passages. A plate fin type heat exchanger characterized in that selected plates having different plate thicknesses are used in the same heat exchanger.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2463293U JPH0684176U (en) | 1993-04-13 | 1993-04-13 | Plate fin type heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2463293U JPH0684176U (en) | 1993-04-13 | 1993-04-13 | Plate fin type heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0684176U true JPH0684176U (en) | 1994-12-02 |
Family
ID=12143515
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2463293U Pending JPH0684176U (en) | 1993-04-13 | 1993-04-13 | Plate fin type heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0684176U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004177006A (en) * | 2002-11-27 | 2004-06-24 | Japan Climate Systems Corp | Internal heat exchanger |
KR101369421B1 (en) * | 2012-03-13 | 2014-03-03 | 주식회사 동화엔텍 | Plate fin exchanger having the zig |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6256979B2 (en) * | 1980-11-11 | 1987-11-28 | Konishiroku Photo Ind |
-
1993
- 1993-04-13 JP JP2463293U patent/JPH0684176U/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6256979B2 (en) * | 1980-11-11 | 1987-11-28 | Konishiroku Photo Ind |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004177006A (en) * | 2002-11-27 | 2004-06-24 | Japan Climate Systems Corp | Internal heat exchanger |
KR101369421B1 (en) * | 2012-03-13 | 2014-03-03 | 주식회사 동화엔텍 | Plate fin exchanger having the zig |
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