JP2548607Y2 - Plate heat exchanger - Google Patents

Plate heat exchanger

Info

Publication number
JP2548607Y2
JP2548607Y2 JP1991107013U JP10701391U JP2548607Y2 JP 2548607 Y2 JP2548607 Y2 JP 2548607Y2 JP 1991107013 U JP1991107013 U JP 1991107013U JP 10701391 U JP10701391 U JP 10701391U JP 2548607 Y2 JP2548607 Y2 JP 2548607Y2
Authority
JP
Japan
Prior art keywords
plate
heat transfer
heat exchanger
container
contact
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.)
Expired - Lifetime
Application number
JP1991107013U
Other languages
Japanese (ja)
Other versions
JPH0552559U (en
Inventor
健二 高橋
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.)
Yazaki Corp
Original Assignee
Yazaki 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 Yazaki Corp filed Critical Yazaki Corp
Priority to JP1991107013U priority Critical patent/JP2548607Y2/en
Publication of JPH0552559U publication Critical patent/JPH0552559U/en
Application granted granted Critical
Publication of JP2548607Y2 publication Critical patent/JP2548607Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は、プレート式熱交換器に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a plate heat exchanger.

【0002】[0002]

【従来の技術】プレート式熱交換器は、一般に複数の伝
熱板を容器内で配列させ、伝熱板間に流体を流動させる
ことにより熱交換を行うものとされている。伝熱板に
は、流体の流路形成及び組み立て後の強度向上のため、
プレス成形された凹凸の表面形状を有するプレートが用
いられる。
2. Description of the Related Art In a plate heat exchanger, a plurality of heat transfer plates are generally arranged in a vessel, and heat is exchanged by flowing a fluid between the heat transfer plates. In order to improve the strength of the heat transfer plate after forming the fluid flow path and assembling,
A press-formed plate having an uneven surface shape is used.

【0003】図4にプレートの表面形状の例を示す。同
例における一対のプレート1及びプレート2は、斜め方
向に延在する平面によって凹部と凸部とが交互に形成さ
れてなり、プレート1及びプレート2の表面形状は互い
に線対称とされている。
FIG . 4 shows an example of the surface shape of a plate. The pair of plates 1 and 2 in the same example have concave portions and convex portions formed alternately by planes extending in an oblique direction, and the surface shapes of the plates 1 and 2 are line-symmetric with each other.

【0004】プレート式熱交換器の流体回路構造は、プ
レート1及びプレート2を組み合わせた複数のプレート
対を容器3内に配列させ、隣接するプレート対を互に接
触させてなり、その断面形状を図5に示す。両外側のプ
レートはそれぞれ容器の側面に接触している。図5にお
いて、縦方向に連通する流体回路4の列が形成され、隣
接する流体回路4において液絡することはない。
[0004] The fluid circuit structure of the plate-type heat exchanger is such that a plurality of plate pairs in which a plate 1 and a plate 2 are combined are arranged in a container 3 and adjacent plate pairs are brought into contact with each other. As shown in FIG . Both outer plates are in contact with the sides of the container. In FIG. 5 , a row of fluid circuits 4 communicating in the vertical direction is formed, and no liquid junction occurs in the adjacent fluid circuits 4.

【0005】このような構造により、異なる種類の流体
を同時に熱交換することが可能になる。図6に流体回路
構造を吸収式冷凍機の溶液熱交換器に適用した例を示
す。図6において、横方向が高温液の流路とされ、縦方
向が低温液の流路とされている。流体回路4は図5に示
すように、縦一列おきに高温液回路及び低温液回路とさ
れ、高温液導入口5から流入した高温液は、高温液回路
を通過して熱交換され、高温液導出口6から流出する。
同様に低温液導入口7から流入した低温液は、低温液回
路を通過して熱交換され、低温液導出口8から流出する
ことになる。
[0005] Such a structure makes it possible to simultaneously exchange heat of different types of fluids. FIG. 6 shows an example in which the fluid circuit structure is applied to a solution heat exchanger of an absorption refrigerator. In FIG. 6, the horizontal direction is the flow path of the high-temperature liquid, and the vertical direction is the flow path of the low-temperature liquid. As shown in FIG. 5 , the fluid circuit 4 has a high-temperature liquid circuit and a low-temperature liquid circuit arranged in every other vertical line. It flows out from the outlet 6.
Similarly, the low-temperature liquid flowing from the low-temperature liquid inlet 7 passes through the low-temperature liquid circuit, undergoes heat exchange, and flows out of the low-temperature liquid outlet 8.

【0006】[0006]

【考案が解決しようとする課題】上記のプレート接触構
造においては、隣接するプレート間の接触箇所(その1
つを図5においてxで示す)は交錯する凸部稜線の交点
であり、すなわちプレート間は点接触となる。一方、両
外側のプレートと容器3の側面との接触箇所(その1つ
を図5においてyで示す)は、それぞれ凸部稜線全体が
容器3側面に接触し、すなわち線接触になる。
In the above-mentioned plate contact structure, the contact point between adjacent plates (part 1)
5 are indicated by x in FIG. 5), which are the intersections of the intersecting convex ridges, that is, the plates are in point contact. On the other hand, at the contact points between the outer plates and the side surfaces of the container 3 (one of which is indicated by y in FIG. 5), the entire convex ridge line comes into contact with the side surface of the container 3, that is, a line contact is made.

【0007】また、プレートと容器3の側面とで形成さ
れる流体回路4′は隣接するプレート間に形成される流
体回路4に対し、容積が1/2となるため、流体回路
4′における流体流動の効率は低下する。
The fluid circuit 4 'formed by the plate and the side surface of the container 3 has a volume half that of the fluid circuit 4 formed between the adjacent plates. The efficiency of the flow decreases.

【0008】このように、流体回路4′はプレートと容
器3の側面と接線に汚染物が堆積し易い構造であり、そ
れにより、プレートが腐食し、異なる流体の液絡が発生
する可能性があった。
As described above, the fluid circuit 4 'has a structure in which contaminants easily accumulate on the plate, the side surface and the tangent of the container 3, whereby the plate may be corroded and a liquid junction of a different fluid may occur. there were.

【0009】本考案は、上記課題に鑑みてなされたもの
で、プレートと容器の側面との間の接触構造を改良し、
汚染物の堆積、それによるプレートの腐食破損、流体の
液絡を防止することを目的とする。
The present invention has been made in view of the above-mentioned problems, and has an improved contact structure between a plate and a side surface of a container.
The purpose of the present invention is to prevent the accumulation of contaminants, the corrosion damage of the plate, and the liquid junction of the fluid.

【0010】[0010]

【課題を解決するための手段】本考案は、凹凸が形成さ
れた複数の伝熱板を容器内に配列させ、各伝熱板の凸部
をそれぞれ隣接する他の伝熱板の凸部に接触させて固定
することにより流体回路を形成してなるプレート式熱交
換器において、容器の側面と、側面に隣接する伝熱板と
の間に、前記伝熱板と点接触し、該伝熱板と前記容器の
側面との間に流体流路となる空間を形成する板状部材を
介在させたことを特徴とする。
According to the present invention, a plurality of heat transfer plates having irregularities are arranged in a container, and the protrusions of each heat transfer plate are respectively arranged on the protrusions of other adjacent heat transfer plates. In a plate heat exchanger in which a fluid circuit is formed by contacting and fixing, a point contact is made between the side surface of the container and a heat transfer plate adjacent to the side surface with the heat transfer plate, and the heat transfer is performed. Plate and said container
It is characterized in that a plate-like member forming a space serving as a fluid flow path is interposed between the side surface and the side surface .

【0011】板状部材は伝熱板と同一形状のダミープレ
ートであり、ダミープレートを隣接する伝熱板に、伝熱
板相互と同様に接触させて配置してもよく、または板状
部材をメッシュ材とし、メッシュ材のメッシュ構造の壁
材の端面を前記伝熱板の凸部に点接触させて配置しても
よい
The plate-like member is a dummy plate having the same shape as the heat transfer plate, and the dummy plate may be arranged in contact with the adjacent heat transfer plate in the same manner as the heat transfer plates. Mesh material , mesh material mesh structure wall
Even if the end face of the material is placed in point contact with the projection of the heat transfer plate,
Good .

【0012】[0012]

【作用】上記構成によると、プレートと容器の側面と
は、線接触せず、汚染物の堆積が抑制される。
According to the above configuration, the plate and the side surface of the container do not come into line contact with each other, and the accumulation of contaminants is suppressed.

【0013】実施例1の構成においては、ダミープレー
トと容器の側面とで形成される流路を熱交換のための流
体回路とせずに、隣接する流体回路に流動する流体と同
一の流体を流動させると、プレートの腐食、破損しても
異なる流体が液絡することはない。
In the configuration of the first embodiment, the flow path formed by the dummy plate and the side surface of the container is not used as a fluid circuit for heat exchange, and the same fluid as the fluid flowing to the adjacent fluid circuit flows. Then, even if the plate is corroded or damaged, a different fluid does not liquid-junction.

【0014】実施例2の構成においては、プレートとメ
ッシュ材との接触は、図3に示すように点接触となり、
汚染物の堆積箇所は低減する。
In the configuration of the second embodiment, the contact between the plate and the mesh material is a point contact as shown in FIG.
Contaminant deposits are reduced.

【0015】[0015]

【実施例】以下、本考案の実施例を図面を参照して説明
する。なお、上記説明と同一の部材には同一の符号を付
して説明を省略する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings. The same members as those described above are denoted by the same reference numerals, and description thereof will be omitted.

【0016】図1は本考案の実施例1の流体回路4及び
プレート接触構造を示し、プレートと容器3側面との間
にダミープレート9が介在している。ダミープレート9
は、プレート1またはプレート2と同一であって隣接す
るプレートと対の形状とされている。すなわち、ダミー
プレート9の接触は、構造的には従来と同一とされる。
ダミープレート9と容器3側面との間に形成される空
間は、熱交換回路とされず、隣接する溶液回路4と同一
の溶液が流動する。
FIG. 1 shows a fluid circuit 4 and a plate contact structure according to a first embodiment of the present invention. A dummy plate 9 is interposed between the plate and the side of the container 3. Dummy plate 9
Is identical to the plate 1 or the plate 2 and is paired with an adjacent plate. That is, the contact of the dummy plate 9 is structurally the same as in the related art.
The space formed between the dummy plate 9 and the side of the container 3 is not a heat exchange circuit, and the same solution flows in the adjacent solution circuit 4.

【0017】本実施例によると、ダミープレート9に汚
染物が堆積し、プレート9が腐食破損しても隣接する溶
液回路4と同一の溶液が流動しているので、異なる溶液
が混合することはなく、熱交換サイクルに支障が生じる
こともない。
According to this embodiment, even if contaminants are deposited on the dummy plate 9 and the plate 9 is corroded and damaged, the same solution flows in the adjacent solution circuit 4, so that different solutions cannot be mixed. And there is no hindrance to the heat exchange cycle.

【0018】図2は本考案の実施例2の流体回路4及び
プレート接触構造を示し、プレートと容器3側面との間
にメッシュ材10が介在している。メッシュ材10はプ
レートの凹凸と異なる表面形状とされ、例えばプレート
2にメッシュ材10を組み合わせると、図3に示すよう
にプレート2とメッシュ材10とは点接触する。従って
汚染物の堆積箇所は低減し、汚染物の堆積、それによる
プレートの腐食破損、異なる溶液の液絡を抑制すること
ができる。
FIG. 2 shows a fluid circuit 4 and a plate contact structure according to a second embodiment of the present invention. A mesh member 10 is interposed between the plate and the side of the container 3. The mesh material 10 has a surface shape different from the unevenness of the plate. For example, when the mesh material 10 is combined with the plate 2, the plate 2 and the mesh material 10 come into point contact as shown in FIG. Therefore, the number of places where contaminants are deposited can be reduced, and the deposition of contaminants, corrosion damage of the plate, and liquid junction of different solutions can be suppressed.

【0019】なお、メッシュ材10の材質はプレートと
同一でよいが、テフロン等の耐食性、電気絶縁性に優れ
た材質とすると、さらに有効である。
The material of the mesh member 10 may be the same as that of the plate. However, it is more effective to use a material having excellent corrosion resistance and electrical insulation such as Teflon.

【0020】[0020]

【考案の効果】以上のように本考案によると、プレート
と容器と間における汚染物の堆積が抑制され、それによ
りプレートの腐食破損、ひいては流体の液絡を防止し
て、耐久性を向上できる等の効果が奏される。本考案
は、プレート溶接のような分解清掃が不可能なプレート
支持構造において、特に有効である。
As described above, according to the present invention, the accumulation of contaminants between the plate and the container is suppressed, thereby preventing corrosion damage of the plate and, consequently, liquid junction of the fluid, thereby improving durability. And the like. The present invention is particularly effective in a plate support structure that cannot be disassembled and cleaned, such as plate welding.

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

【図1】本考案の実施例1による流体回路及び伝熱板接
触構造を示す断面図である。
FIG. 1 is a sectional view illustrating a fluid circuit and a heat transfer plate contact structure according to a first embodiment of the present invention;

【図2】本考案の実施例2による流体回路及び伝熱板接
触構造を示す断面図である。
FIG. 2 is a cross-sectional view illustrating a fluid circuit and a heat transfer plate contact structure according to a second embodiment of the present invention;

【図3】実施例2のプレート及びメッシュ板材の組み合
わせを示す説明図である。
FIG. 3 is an explanatory diagram showing a combination of a plate and a mesh plate material according to a second embodiment.

【図4】伝熱板のプレート表面形状を示す平面図であ
る。
FIG. 4 is a plan view showing a plate surface shape of a heat transfer plate.

【図5】従来の技術の一例による流体回路及び伝熱板接
触構造を示す断面図である。
FIG. 5 is a cross-sectional view illustrating a fluid circuit and a heat transfer plate contact structure according to an example of the related art.

【図6】流体回路を吸収式冷凍機の溶液熱交換器に適用
した例を示す斜視図である。
FIG. 6 is a perspective view showing an example in which the fluid circuit is applied to a solution heat exchanger of an absorption refrigerator.

【符号の説明】[Explanation of symbols]

1 プレート 2 プレート 3 容器 4、4′ 流体回路 5 高温液導入口 6 高温液導出口 7 低温液導入口 8 低温液導出口 9 ダミープレート 10 メッシュ材 Reference Signs List 1 plate 2 plate 3 container 4, 4 'fluid circuit 5 high-temperature liquid inlet 6 high-temperature liquid outlet 7 low-temperature liquid inlet 8 low-temperature liquid outlet 9 dummy plate 10 mesh material

Claims (3)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 凹凸が形成された複数の伝熱板を容器内
に配列させ、各伝熱板の凸部をそれぞれ隣接する他の伝
熱板の凸部に接触させて固定することにより流体回路を
形成してなるプレート式熱交換器において、前記容器の
側面と、該側面に隣接する前記伝熱板との間に、前記伝
熱板と点接触し、該伝熱板と前記容器の側面との間に流
体流路となる空間を形成する板状部材を介在させたこと
を特徴とするプレート式熱交換器。
A fluid is formed by arranging a plurality of heat transfer plates having irregularities in a container and contacting and fixing the protrusions of each heat transfer plate with the protrusions of another adjacent heat transfer plate. in plate heat exchanger obtained by forming a circuit, between a side surface of the container, and the heat transfer plate adjacent to the side surface, the heat transfer
Point contact with the hot plate, and flow between the heat transfer plate and the side of the vessel
A plate heat exchanger comprising a plate-like member forming a space serving as a body flow path interposed therebetween.
【請求項2】 前記板状部材は前記伝熱板と同一形状の
ダミープレートであり、ダミープレートを隣接する前記
伝熱板に、伝熱板相互と同様に接触させて配置したこと
を特徴とする請求項1に記載のプレート式熱交換器。
2. The method according to claim 1, wherein the plate-like member is a dummy plate having the same shape as the heat transfer plate, and the dummy plate is arranged in contact with the adjacent heat transfer plate in the same manner as the heat transfer plates. The plate heat exchanger according to claim 1.
【請求項3】 前記板状部材はメッシュ材であり、該メ
ッシュ材のメッシュ構造の壁材の端面を前記伝熱板の凸
部に点接触させて配置したことを特徴とする請求項1に
記載のプレート式熱交換器
Wherein said plate-like member is a mesh material,該Me
The end face of the mesh material of the mesh material
2. The method according to claim 1, wherein the first and second portions are arranged in point contact with each other.
The plate heat exchanger as described .
JP1991107013U 1991-12-25 1991-12-25 Plate heat exchanger Expired - Lifetime JP2548607Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991107013U JP2548607Y2 (en) 1991-12-25 1991-12-25 Plate heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991107013U JP2548607Y2 (en) 1991-12-25 1991-12-25 Plate heat exchanger

Publications (2)

Publication Number Publication Date
JPH0552559U JPH0552559U (en) 1993-07-13
JP2548607Y2 true JP2548607Y2 (en) 1997-09-24

Family

ID=14448295

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991107013U Expired - Lifetime JP2548607Y2 (en) 1991-12-25 1991-12-25 Plate heat exchanger

Country Status (1)

Country Link
JP (1) JP2548607Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02230087A (en) * 1989-02-28 1990-09-12 Daikin Ind Ltd Heat exchanger

Also Published As

Publication number Publication date
JPH0552559U (en) 1993-07-13

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