JP3443610B2 - Plate heat exchanger - Google Patents

Plate heat exchanger

Info

Publication number
JP3443610B2
JP3443610B2 JP24233893A JP24233893A JP3443610B2 JP 3443610 B2 JP3443610 B2 JP 3443610B2 JP 24233893 A JP24233893 A JP 24233893A JP 24233893 A JP24233893 A JP 24233893A JP 3443610 B2 JP3443610 B2 JP 3443610B2
Authority
JP
Japan
Prior art keywords
plates
adjacent
heat exchanger
ridges
plate heat
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 - Fee Related
Application number
JP24233893A
Other languages
Japanese (ja)
Other versions
JPH0798191A (en
Inventor
淳一 中村
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.)
Hisaka Works Ltd
Original Assignee
Hisaka Works 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 Hisaka Works Ltd filed Critical Hisaka Works Ltd
Priority to JP24233893A priority Critical patent/JP3443610B2/en
Publication of JPH0798191A publication Critical patent/JPH0798191A/en
Application granted granted Critical
Publication of JP3443610B2 publication Critical patent/JP3443610B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、横畝形状の伝熱面を有
するプレートを用いたプレート式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 plate heat exchanger using a plate having a horizontal ridge-shaped heat transfer surface.

【0002】[0002]

【従来の技術】一般に、プレート式熱交換器は、複数枚
のプレートをガスケットを介して積層してプレート相互
間に複数の媒体通路を形成し、この複数の媒体通路に熱
交換されるべき異なる熱交換媒体を交互に流通して両熱
交換媒体間でプレートを介して熱交換を行わせる。
2. Description of the Related Art Generally, a plate type heat exchanger has a plurality of plates laminated with a gasket interposed therebetween to form a plurality of medium passages between the plates, and the plurality of medium passages are different in heat exchange. The heat exchange media are alternately flowed to exchange heat between the two heat exchange media via a plate.

【0003】 このようなプレート式熱交換器において
は、例えば、図3に示す如き、プレート(1)が使用さ
れている。このプレート(1)は、長方形に形成され、
中央部に伝熱面(2)を有し、かつ、4隅に熱交換媒体
の出入口となる孔(3a)(3b)(3c)(3d)が
夫々穿設されている。また、プレート(1)には、伝熱
面(2)の周囲および各孔(3a)(3b)(3c)
(3d)の周囲を囲繞する部分にガスケット溝(4)が
形成してあり、このガスケット溝(4)に、伝熱面
(2)および一対の上下の孔(3a)(3b)を連通
し、かつ、他の一対の上下の孔(3c)(3d)を遮断
するようにガスケット(5)が装着されている。
In such a plate heat exchanger, for example, a plate (1) as shown in FIG. 3 is used. This plate (1) is formed in a rectangular shape,
It has a heat transfer surface (2) in the center, and holes (3a) (3b) (3c) (3d) serving as inlets and outlets of the heat exchange medium are formed at four corners. Further, the plate (1) has a periphery of the heat transfer surface (2) and holes (3a) (3b) (3c).
A gasket groove (4) is formed in a portion surrounding the periphery of (3d), and the heat transfer surface (2) and a pair of upper and lower holes (3a) (3b) are communicated with the gasket groove (4). A gasket (5) is attached so as to block the other pair of upper and lower holes (3c) (3d).

【0004】そして、上記プレート(1)の伝熱面
(2)は、図4に示すように、伝熱性能の向上とプレー
ト強度の向上を図るため、多数の横畝(6)を並列状に
配設して例えば台形状の断面の凸凹が交互に続く横畝形
状に形成されており、横畝(6)(6)間の任意の位置
に形成した縦畝(7)で隣接するプレート(1’)の横
畝(6’)(6’)間の底面を支持することによってプ
レート(1)(1’)間の間隔を保持するようにしてい
る。
As shown in FIG. 4, the heat transfer surface (2) of the plate (1) has a large number of horizontal ridges (6) arranged in parallel in order to improve heat transfer performance and plate strength. Is formed in a horizontal ridge shape in which trapezoidal cross-section irregularities are alternately arranged and adjacent plates are formed by vertical ridges (7) formed at arbitrary positions between the horizontal ridges (6) and (6). The space between the plates (1) and (1 ') is maintained by supporting the bottom surface between the horizontal ridges (6') and (6 ') of (1').

【0005】[0005]

【発明が解決しようとする課題】ところで、多数の横畝
(6)を並列状に配設した横畝形状の伝熱面(2)を有
するプレート(1)は、上述した如く、横畝(6)
(6)間の任意位置に形成した縦畝(7)で隣接するプ
レート(1’)の横畝(6’)(6’)間の底面を支持
することによってプレート相互(1)(1’)間の間隔
を保持するようにしている。
By the way, the plate (1) having the horizontal ridge-shaped heat transfer surface (2) in which a large number of horizontal ridges (6) are arranged in parallel is, as described above, a horizontal ridge ( 6)
By supporting the bottom surface between the horizontal ridges (6 ') (6') of the adjacent plates (1 ') by the vertical ridges (7) formed at arbitrary positions between the plates (1) (1'). ) I try to keep the space between them.

【0006】ところが、横畝(6)(6)間の任意位置
に形成した縦畝(7)で隣接するプレート(1)の横畝
(6’)(6’)間の底面を支持するプレート相互間の
支持点(8)では、スケール性を有する流体が流れた場
合には、支持点(8)の隙間にスケールが付着し、ま
た、薬液等の洗浄時においても支持点(8)に付着する
スケールが充分に除去できない。そのため、食品用途で
は洗浄後に残存したスケールが雑菌の繁殖床となり、衛
生面で問題がある。
However, a plate that supports the bottom surface between the horizontal ridges (6 ') (6') of the adjacent plates (1) by the vertical ridges (7) formed at arbitrary positions between the horizontal ridges (6) (6). At the mutual support points (8), when a fluid having a scale property flows, the scale adheres to the gap between the support points (8), and also at the time of cleaning with a chemical solution, etc. The adhered scale cannot be removed sufficiently. Therefore, in food applications, the scale remaining after washing becomes a breeding bed for miscellaneous bacteria, which is a sanitary problem.

【0007】また、一般用途での腐食性の強い流体の場
合には、支持点(8)の隙間部に多量のスケールが付着
することによって金属の隙間腐食を誘発する原因になる
問題がある。
Further, in the case of a fluid having a strong corrosive property for general use, there is a problem that a large amount of scale adheres to the gap portion of the support point (8) to induce crevice corrosion of metal.

【0008】 これらの問題点の発生要因は、図4
(b)に示す如き支持点(8)のない流路に比べて、図
4(c)に示す如き支持点(8)のある流路では、支持
点(8)によって流路が部分的に閉塞されて流速が遅く
なり、この遅い流速では支持点(8)の隙間にスケール
が付着しやすいし、また、洗浄時においても支持点
(8)に付着するスケールを除去し難いためである。
The cause of these problems is shown in FIG.
Compared to the flow channel without the support points (8) as shown in (b), the flow channel with the support points (8) as shown in FIG. This is because the flow velocity becomes slow due to blockage, and at this low flow velocity, the scale easily adheres to the gap between the supporting points (8) and it is difficult to remove the scale adhering to the supporting points (8) even during cleaning.

【0009】本発明は上記問題点に鑑みて提案されたも
ので、プレート相互間の支持点でのスケールの付着を抑
制するとともに洗浄効果を助長するプレート式熱交換器
を提供することを目的とするものである。
The present invention has been proposed in view of the above problems, and an object thereof is to provide a plate heat exchanger that suppresses adhesion of scales at support points between plates and promotes a cleaning effect. To do.

【0010】[0010]

【課題を解決するための手段】本発明は上記目的を達成
するため、多数の横畝を並列状に配設した伝熱面を有す
る複数枚のプレートを積層し、上記横畝間の任意位置に
形成した縦畝で隣接するプレートの横畝間の底面を支持
することによつてプレート相互間の間隔を保持するプレ
ート式熱交換器において、プレート相互間の支持点に隣
接する横側方あるいは横側方の縦縦延長線上を流体の流
れに概沿った縦溝構造に形成したものである。
In order to achieve the above-mentioned object, the present invention laminates a plurality of plates having a heat transfer surface in which a large number of horizontal ridges are arranged in parallel, and places them at arbitrary positions between the horizontal ridges. In a plate heat exchanger that maintains the space between the plates by supporting the bottom surface between the horizontal ridges of the adjacent plates with the formed vertical ridges, the lateral side or the lateral side adjacent to the support point between the plates One of the vertical and vertical extension lines is formed in a vertical groove structure that is substantially along the fluid flow.

【0011】[0011]

【作用】プレート相互間の支持点に隣接する横側方ある
いは横側方の縦延長線上を流体の流れに概沿った縦溝構
造に形成したから、この縦溝構造部において流速の速い
流れが得られ、この速い流れがプレート相互間の支持点
に隣接するため、この速い流れによりプレート相互間の
支持点に付着するスケールを剥離することができる。
[Function] Since a vertical groove structure is formed along the lateral side or the lateral extension line adjacent to the supporting point between the plates, the flow path having a high flow velocity is formed in the vertical groove structure portion. As a result, this fast flow is adjacent to the support points between the plates, so that the fast flow can separate scales that attach to the support points between the plates.

【0012】[0012]

【実施例】以下、本発明に係るプレート式熱交換器の各
実施例について図1および図2に基づいて説明する。
尚、図3および図4に示したものと同一部材乃至同一部
分には同一符号を付し、重複する事項の説明を省略す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Each embodiment of the plate heat exchanger according to the present invention will be described below with reference to FIGS.
The same members or parts as those shown in FIGS. 3 and 4 are designated by the same reference numerals, and a duplicate description will be omitted.

【0013】図1は本発明の第1実施例を示しており、
プレート(1)の横畝(6)(6)間の任意位置に形成
した縦畝(7)に隣接する横側方に横畝(6)を縦断す
る縦溝(9)を形成することにより、隣接するプレート
(1’)との支持点(8)に隣接する横側方部を流体の
流れに概沿った縦溝構造に形成したものである。
FIG. 1 shows a first embodiment of the present invention,
By forming a vertical groove (9) longitudinally crossing the horizontal ridge (6) adjacent to the vertical ridge (7) formed at an arbitrary position between the horizontal ridges (6) (6) of the plate (1) , A lateral side portion adjacent to a supporting point (8) with an adjacent plate (1 ′) is formed in a vertical groove structure that is substantially along the fluid flow.

【0014】 本実施例のプレート式熱交換器において
は、プレート(1)(1’)間の支持点(8)に隣接す
る横側方部を縦溝(9)により、図1(b)に示すよう
に、流体の流れに概沿った縦溝構造に形成したので、こ
の縦溝構造部では他の図1(c)に示す如き折れ曲がっ
た流路、あるいは図1(d)に示す如き支持点(8)の
ある流路に比べて流体の圧力損失が少ないため、多量で
流速の早い流れが得られる。そして、この多量で流速の
速い流れがプレート(1)(1’)間の支持点(8)に
隣接するため、この速い流れによりプレート(1)
(1’)間の支持点(8)に付着しようとするスケール
を流れの物理的力で剥離し、支持点(8)へのスケール
の付着を抑制する。また、この速い流れは薬液等の洗浄
時においてもプレート(1)(1’)間の支持点(8)
に付着成長するスケールを剥離する効果があり、高い洗
浄効果が得られる。
In the plate heat exchanger of this embodiment, the lateral side portion adjacent to the support point (8) between the plates (1) and (1 ′) is formed by the vertical groove (9), as shown in FIG. As shown in FIG. 2, since the vertical groove structure is formed along the flow of the fluid, the vertical groove structure portion has another bent channel as shown in FIG. 1 (c), or as shown in FIG. 1 (d). Since the pressure loss of the fluid is smaller than that of the flow path having the support points (8), a large amount of a high-speed flow can be obtained. Since this large amount of high-speed flow is adjacent to the support point (8) between the plates (1) and (1 ′), the high-speed flow causes the plate (1) to move.
The scale that tends to adhere to the support points (8) between (1 ′) is separated by the physical force of the flow, and the scale adhesion to the support points (8) is suppressed. In addition, this fast flow is due to the support point (8) between the plates (1) and (1 ') even when cleaning the chemical solution.
It has the effect of exfoliating the scale that adheres to and grows, and a high cleaning effect can be obtained.

【0015】図2は本発明の第2実施例を示しており、
プレート(1)の横畝(6)(6)間の任意位置に形成
した縦畝(7)に隣接する横側方の縦延長線上に対向し
て隣接するプレート(1’)に縦畝(7’)を形成する
ことにより、プレート(1)(1’)の支持点(8)に
隣接する横側方の縦延長線上を流体の流れに概沿った縦
溝構造に形成したものであり、作用効果は図1に示す第
1実施例と同じである。
FIG. 2 shows a second embodiment of the present invention,
Longitudinal ridges (along the ridges (6) (6) of the plate (1)) adjacent to the vertical ridges (7) formed at arbitrary positions between the lateral ridges (6) and (6) facing each other on the lateral extension line. 7 ') is formed to form a flute structure along the horizontal flow line on the lateral extension line adjacent to the support point (8) of the plate (1) (1'). The function and effect are the same as those of the first embodiment shown in FIG.

【0016】尚、上記第1および第2実施例において、
隣接し合うプレートは横畝(6)の平面形状の異なる2
種類のプレートを用いてもよいし、また、同一のプレー
トを回転あるいは反転して組み合わせて使用してもよ
い。
In the above first and second embodiments,
Adjacent plates have different horizontal ridges (6) 2
Different types of plates may be used, or the same plate may be rotated or inverted and used in combination.

【0017】また、上記第1および第2の実施例では、
支持点(8)の片側方のみに隣接して縦溝構造を形成し
ているが、支持点(8)の両側方に縦溝(9)を設けて
もよい。
Further, in the first and second embodiments,
Although the vertical groove structure is formed adjacent to only one side of the supporting point (8), the vertical groove (9) may be provided on both sides of the supporting point (8).

【0018】[0018]

【発明の効果】以上説明したように、本発明は、プレー
ト相互間の支持点に隣接する横側方あるいは横側方の縦
延長線上を流体の流れに概沿った縦溝構造に形成し、こ
の縦溝構造部における流体の流れを速くしたから、この
速い流れによりプレート相互間の支持点に付着するスケ
ールを剥離でき、プレート相互間の支持点でのスケール
の付着を抑制するとともに洗浄効果を助長することがで
きる。
As described above, according to the present invention, the lateral groove adjacent to the supporting points between the plates or the lateral lateral vertical extension line is formed into a flute structure that is substantially along the fluid flow, Since the fluid flow in this flute structure is made faster, the scale that adheres to the support points between the plates can be separated by this fast flow, and the adhesion of scale at the support points between the plates can be suppressed and the cleaning effect can be improved. Can be encouraged.

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

【図1】 本発明のプレート式熱交換器の第1実施例を
示す図面であり、(a)はプレートの要部平面図、
(b)(c)(d)および(e)は隣接するプレートを
積層した状態での(a)のb−b線、c−c線、d−d
線およびe−e線における断面図である。
FIG. 1 is a view showing a first embodiment of a plate heat exchanger of the present invention, (a) is a plan view of a main part of a plate,
(B), (c), (d), and (e) are bb line, cc line, and dd line of (a) in a state where adjacent plates are laminated.
It is sectional drawing in the line and ee line.

【図2】 本発明のプレート式熱交換器の第2実施例を
示す図面であり、(a)は一方のプレートの要部平面
図、(b)は隣接するプレートの要部平面図、(c)お
よび(d)は一方のプレートと隣接するプレートを積層
した状態での(a)および(b)でのc−c線およびd
−d線における断面図である。
2A and 2B are drawings showing a second embodiment of the plate heat exchanger of the present invention, where FIG. 2A is a plan view of a main part of one plate, FIG. 2B is a plan view of a main part of an adjacent plate, c) and (d) are cc line and d in (a) and (b) in the state where one plate and an adjacent plate are laminated.
It is sectional drawing in the -d line.

【図3】 プレート式熱交換器に使用するプレートの平
面図である。
FIG. 3 is a plan view of a plate used in the plate heat exchanger.

【図4】 従来のプレート式熱交換器を示す図面であ
り、(a)はプレートの要部平面図、(b)(c)およ
び(d)は隣接するプレートを積層した状態での(a)
のb−b線、c−c線およびd−d線における断面図で
ある。
FIG. 4 is a view showing a conventional plate heat exchanger, in which (a) is a plan view of an essential part of the plate, and (b), (c) and (d) show (a) a state in which adjacent plates are laminated. )
3 is a cross-sectional view taken along line bb, cc, and dd of FIG.

【符号の説明】[Explanation of symbols]

1 プレート 1’ 隣接するプレート 2 伝熱面 6 横畝 6’ 横畝 7 縦畝 7’ 縦畝 8 支持点 9 縦溝 1 plate 1'adjacent plates 2 Heat transfer surface 6 horizontal ridges 6'side ridge 7 vertical ridges 7'longitudinal ridge 8 support points 9 flutes

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 多数の横畝を並列状に配設した伝熱面を
有する複数枚のプレートを積層し、上記横畝間の任意位
置に形成した縦畝で隣接するプレートの横畝間の底面を
支持することによつてプレート相互間の間隔を保持する
プレート式熱交換器において、 プレート相互間の支持点に隣接する横側方あるいは横側
方の縦延長線上を流体の流れに概沿った縦溝構造に形成
したことを特徴とするプレート式熱交換器。
1. A plurality of plates having a heat transfer surface in which a large number of horizontal ridges are arranged in parallel are laminated, and a vertical ridge formed at an arbitrary position between the horizontal ridges forms a bottom face between the horizontal ridges of adjacent plates. In a plate heat exchanger that maintains the distance between the plates by supporting them, in the lateral direction that is adjacent to the supporting point between the plates or on the vertical extension line of the lateral side that is generally along the fluid flow. A plate heat exchanger having a groove structure.
【請求項2】 プレートの縦畝に隣接する横側方に横畝
を縦断する縦溝を形成することにより、プレート相互間
の支持点に隣接する横側方を流体の流れに概沿った縦溝
構造に形成したことを特徴とする請求項1のプレート式
熱交換器。
2. A longitudinal groove that cuts the horizontal ridges is formed on the lateral side adjacent to the longitudinal ridges of the plates, so that the lateral side adjacent to the supporting points between the plates is aligned with the fluid flow. The plate heat exchanger according to claim 1, wherein the plate heat exchanger has a groove structure.
【請求項3】 プレートの縦畝に隣接する横側方の縦延
長線上に対向して隣接するプレートに縦畝を形成するこ
とにより、プレート相互間の支持点に隣接する横側方の
縦延長線上を流体の流れに概沿った縦溝構造に形成した
ことを特徴とする請求項1のプレート式熱交換器。
3. A vertical lateral extension adjacent to a supporting point between the plates by forming vertical ridges on the adjacent plates facing each other on a lateral lateral extension line adjacent to the vertical ridges of the plates. 2. The plate heat exchanger according to claim 1, wherein a flute structure is formed on the line along the flow of the fluid.
JP24233893A 1993-09-29 1993-09-29 Plate heat exchanger Expired - Fee Related JP3443610B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24233893A JP3443610B2 (en) 1993-09-29 1993-09-29 Plate heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24233893A JP3443610B2 (en) 1993-09-29 1993-09-29 Plate heat exchanger

Publications (2)

Publication Number Publication Date
JPH0798191A JPH0798191A (en) 1995-04-11
JP3443610B2 true JP3443610B2 (en) 2003-09-08

Family

ID=17087714

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24233893A Expired - Fee Related JP3443610B2 (en) 1993-09-29 1993-09-29 Plate heat exchanger

Country Status (1)

Country Link
JP (1) JP3443610B2 (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1197933A (en) * 1967-09-18 1970-07-08 Apv Co Ltd Improvements in or relating to Plate Type Heat Exchangers
JPS5710353B2 (en) * 1972-12-21 1982-02-25
JPS61186794A (en) * 1985-02-15 1986-08-20 Hisaka Works Ltd Plate type heat exchanger
SE458806B (en) * 1987-04-21 1989-05-08 Alfa Laval Thermal Ab PLATE HEAT EXCHANGER WITH DIFFERENT FLOW RESISTANCE FOR MEDIA

Also Published As

Publication number Publication date
JPH0798191A (en) 1995-04-11

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