JPH0833286B2 - Plate type heat exchanger - Google Patents

Plate type heat exchanger

Info

Publication number
JPH0833286B2
JPH0833286B2 JP61299378A JP29937886A JPH0833286B2 JP H0833286 B2 JPH0833286 B2 JP H0833286B2 JP 61299378 A JP61299378 A JP 61299378A JP 29937886 A JP29937886 A JP 29937886A JP H0833286 B2 JPH0833286 B2 JP H0833286B2
Authority
JP
Japan
Prior art keywords
heat transfer
heat
heat exchanger
plate
gaps
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
JP61299378A
Other languages
Japanese (ja)
Other versions
JPS63150591A (en
Inventor
敏一 八木
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 JP61299378A priority Critical patent/JPH0833286B2/en
Publication of JPS63150591A publication Critical patent/JPS63150591A/en
Publication of JPH0833286B2 publication Critical patent/JPH0833286B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 この発明は二系統の流体通路を有するプレート式熱交
換器に関し、特に、流体同士が混ざり合うことを避けな
ければならない場合でも支障なく利用できるようにした
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 having two fluid passages, and particularly, it can be used without trouble even when it is necessary to avoid mixing fluids. Plate type heat exchanger.

従来の技術 従来のプレート式熱交換器は第3図に示すように、一
枚の伝熱板からなる伝熱エレメント(p)(p′)を介
して二系統の流体通路(A)(B)が隣接しており、こ
の伝熱エレメントを介して間接的に、流体相互間の熱交
換が行われることは周知の通りである。プレート式熱交
換器の一例として特開昭61−122493号公報に記載のもの
を挙げることができる。
2. Description of the Related Art As shown in FIG. 3, a conventional plate heat exchanger has two fluid passages (A) and (B) via heat transfer elements (p) and (p ') each including one heat transfer plate. ) Are adjacent to each other, and heat exchange between fluids is indirectly performed via the heat transfer element, as is well known. As an example of the plate heat exchanger, the one described in JP-A-61-212493 can be mentioned.

発明が解決しようとする問題点 プレート式熱交換器は多数の伝熱エレメントが成層し
た構造であるため、腐食等により伝熱壁に万一穴が開い
ても容易には発見できず、その結果、被処理液飲用水に
熱媒体が混入してしまうといった不都合が生ずる。
Problems to be Solved by the Invention Since the plate heat exchanger has a structure in which a large number of heat transfer elements are layered, even if a hole is opened in the heat transfer wall due to corrosion or the like, it cannot be easily found. However, there arises a disadvantage that the heat medium is mixed into the drinking water to be treated.

したがって、液質を保証する上からは、このような異
常を未然に発見して異流体の混入を防止することが要求
される。しかしてチューブ式の熱交換器においては、伝
熱チューブを二重にして二重隔壁間に、漏れ確認のため
の通水を実施する間隙を設けることも行われている(実
開昭57−120874号公報)。
Therefore, in order to guarantee the liquid quality, it is required to detect such abnormalities in advance and prevent the mixing of different fluids. However, in the tube type heat exchanger, the heat transfer tubes are doubled and a gap is provided between the double partition walls so as to confirm water leakage (actual exploitation 57- 120874 publication).

しかしながら、二重の隔壁を介してしかも両隔壁間に
空気が存在している状態での熱伝達は効率が非常に悪
く、伝熱性能を犠牲にすることになり、実用化が阻まれ
ていたものである。
However, the efficiency of heat transfer through the double partition walls and in the presence of air between both partition walls is very poor, and the heat transfer performance is sacrificed, which impedes practical application. It is a thing.

そこでこの発明は、以上述べたような問題点を解消せ
んとするもので、すなわち、所期の伝熱性能を確保しつ
つ、万一腐食等により伝熱壁に穴が開いても、流体が混
ざり合うことのないようなプレート式熱交換器を提供す
ることを目的としている。
Therefore, the present invention is intended to solve the problems as described above, that is, while ensuring the desired heat transfer performance, even if a hole is opened in the heat transfer wall due to corrosion or the like, the fluid will not flow. It is an object of the present invention to provide a plate heat exchanger that does not mix with each other.

問題点を解決するための手段 この発明は、伝熱エレメントを介して隣接する二系統
の流体通路内の流体相互間で熱交換が行われるものにお
いて、伝熱エレメントを一対の伝熱体相互間で熱交換が
行われるものにおいて、伝熱エレメントを一対の伝熱板
で構成し、前記伝熱板を水密でない程度の隙間を残して
互いに接触させるとともに外周で前記隙間を外部に開放
させ、流体の出入口となる貫通孔の周囲において水密に
接合し、前記隙間と連通させて注水口および排水受を設
け、かつ、前記対の伝熱板の伝熱部を互いに部分的にろ
う付けすることによって上記の課題を解決したものであ
る。
Means for Solving the Problems The present invention relates to a method in which heat is exchanged between fluids in two adjacent fluid passages via a heat transfer element, and the heat transfer element is provided between a pair of heat transfer elements. In the one in which heat exchange is performed in, the heat transfer element is composed of a pair of heat transfer plates, and the heat transfer plates are brought into contact with each other leaving a gap that is not watertight, and at the outer periphery, the gap is opened to the outside. By water-tightly joining around the through-hole serving as the entrance and exit of the above, providing a water injection port and a drain receiver in communication with the gap, and partially brazing the heat transfer parts of the pair of heat transfer plates to each other. This is a solution to the above problem.

作用 伝熱板間に残された外部に開放した隙間を利用して、
必要に応じて、通水等をすることにより漏れの有無等を
確認することができる。
Using the open gap left between the heat transfer plates,
If necessary, it is possible to confirm the presence or absence of leakage by passing water or the like.

流体相互間の熱交換は伝熱エレメントを介して間接的
に行われるが、伝熱エレメントを構成する伝熱板間の隙
間は水密でない程度にしてあるので、伝熱性能を著しく
損なうことはない。さらに、ろう付けによって伝熱板の
熱伝導率が向上し、伝熱性能を積極的に確保する。
Heat exchange between fluids is indirectly performed via the heat transfer element, but the gap between the heat transfer plates that make up the heat transfer element is not watertight, so heat transfer performance is not significantly impaired. . Further, the heat conductivity of the heat transfer plate is improved by brazing, and the heat transfer performance is positively secured.

実施例 図面に示す実施例について説明すると、第2図A、B
はそれぞれ伝熱エレメント(P)(P′)の正面図であ
って、これらの伝熱エレメント(P)(P′)を第1図
に示すように仕様に応じて所定枚数交互に積層してプレ
ート式熱交換器が構成される。
EXAMPLE An example shown in the drawings will be described with reference to FIGS.
3A and 3B are front views of the heat transfer elements P, P ', respectively. As shown in FIG. 1, these heat transfer elements P, P'are alternately laminated in a predetermined number according to the specifications. A plate heat exchanger is constructed.

各伝熱エレメント(P)(P′)は同一形状の一対の
伝熱板(12)(14)からなり、伝熱板(12)(14)同士
は互いに接触するも相互間に水密でない程度の隙間(1
6)を残しており、この隙間(16)は外部に開放してい
る。なお、図面はこの隙間(16)を相当誇張して示して
いる。伝熱エレメント(P)(P′)は四隅に流体の出
入口(18)(20)(22)(24)を有し、それらの周囲に
おいて参照符号(26)で指すように、伝熱板(12)(1
4)はろう付けその他の適当な手段により水密に接合さ
れ、熱交換流体が隙間(16)に流入しないようになって
いる。
Each heat transfer element (P) (P ') is composed of a pair of heat transfer plates (12) (14) of the same shape, and the heat transfer plates (12) (14) are in contact with each other but are not watertight to each other. Gap (1
6) is left, and this gap (16) is open to the outside. The drawing shows the gap (16) in an exaggerated manner. The heat transfer element (P) (P ') has fluid inlets / outlets (18) (20) (22) (24) at four corners, and a heat transfer plate ( 12) (1
4) is watertightly joined by brazing or other suitable means so that the heat exchange fluid does not flow into the gap (16).

また、伝熱エレメント(P)(P′)の熱伝導率を高
めて伝熱性能を積極的に確保するため、参照符号(32)
で指す箇所は、伝熱板(12)(14)を互いにろう付けし
てある。第2図Aは伝熱部の波形の方向にろう付けした
例を示し、第2図Bは縦方向にろう付けした例を示す。
このほかに散点状に分散した位置でろう付けするなど種
々のパターンを採用することもできる。いずれの場合も
伝熱部を全面にわたって接合するのでなく、隙間(16)
を流体が流下できるように部分的にろう付けしてある。
熱伝導率の高いろう材を選ぶべきことは言うまでもな
い。なお、このろう付けにより伝熱エレメントの剛性が
増すので強度上も有利である。
Further, in order to positively secure the heat transfer performance by increasing the thermal conductivity of the heat transfer element (P) (P '), the reference numeral (32)
Heat transfer plates (12) and (14) are brazed to each other at points indicated by. FIG. 2A shows an example of brazing in the corrugated direction of the heat transfer section, and FIG. 2B shows an example of brazing in the vertical direction.
In addition to this, various patterns such as brazing at scattered points can be adopted. In either case, instead of joining the heat transfer parts over the entire surface, the gap (16)
Is partially brazed to allow the fluid to flow down.
It goes without saying that a brazing material with high thermal conductivity should be selected. This brazing increases the rigidity of the heat transfer element, which is advantageous in terms of strength.

伝熱板(12)(14)は伝熱に実質的に関与する中央の
伝熱部を波形に成形してある。これは隣接する伝熱エレ
メント(P)(P′)間では波形同士が交差衝合して伝
熱エレメントの間隔を保持し、また流体の乱流を促進し
て伝熱効率を向上させる働きをするが、この発明にとっ
ては必須のものというわけではなく、その他の種々の形
状を採用することも勿論可能である。
The heat transfer plates (12) and (14) are formed by corrugating a central heat transfer portion that substantially participates in heat transfer. This is because the corrugations of the adjacent heat transfer elements (P) and (P ') are cross-butted to each other to maintain the space between the heat transfer elements and to promote the turbulent flow of the fluid to improve the heat transfer efficiency. However, it is not essential to the present invention, and it is of course possible to adopt various other shapes.

隣接する伝熱エレメント(P)(P′)同士は伝熱部
の周囲および流体の出入口の周囲において、それぞれ参
照符号(28)(30)で指すように、ろう付けその他の適
当な手段により接合し、或いはガスケットを配設するこ
とによって、流体の器外への漏れおよび流体相互の混合
を防止する。なお、前記の特開昭61−122493号公報に記
載してあるように、伝熱エレメントの外周縁を折曲し
て、いわゆる入れ子式に重合するようにしてもよい。
Adjacent heat transfer elements (P) and (P ') are joined by brazing or other suitable means around the heat transfer section and around the fluid inlet and outlet, as indicated by reference numerals (28) and (30), respectively. Or a gasket is provided to prevent fluid from leaking out of the vessel and mixing with each other. Incidentally, as described in the above-mentioned JP-A-61-212493, the outer peripheral edge of the heat transfer element may be bent so as to polymerize in a so-called nested manner.

次に第1図を参照して熱媒体で被処理液を加熱する場
合の各流体の流れについて述べるならば、熱媒体は伝熱
エレメント(P)(P′)の熱媒体入口(18)から伝熱
エレメント(P)(P′)間の通路(A)に流入し、続
いて熱媒体出口(20)を通って流出する。被処理液の方
は伝熱エレメント(P)(P′)の被処理液入口(22)
から伝熱エレメント(P)(P′)間の通路(B)へ流
入し、続いて被処理液出口(24)から流出する。そうし
てそれぞれ隣接する通路(A)(B)内を流過する間
に、伝熱エレメント(P)(P′)を介して、被処理液
は熱媒体から熱を受け取って昇温する。その際、伝熱エ
レメント(P)(P′)を構成する伝熱板(12)(14)
は密着しているわけではないので一枚のものよりは多少
熱伝達率が劣るものの、完全な空気層が介在する二重隔
壁に比べると伝熱性能を著しく損なうということはな
い。加えて、ろう付け(32)部分が熱伝導に有効に作用
するため、所定の伝熱性能を確保することができる。
Next, referring to FIG. 1, to describe the flow of each fluid when heating the liquid to be treated with the heat medium, the heat medium is introduced from the heat medium inlet (18) of the heat transfer element (P) (P '). It flows into the passage (A) between the heat transfer elements (P) and (P ') and then flows out through the heat medium outlet (20). The liquid to be treated is the liquid to be treated inlet (22) of the heat transfer element (P) (P ').
Flow into the passage (B) between the heat transfer elements (P) and (P ′), and then flow out from the liquid outlet (24) to be treated. Then, the liquid to be treated receives heat from the heat medium via the heat transfer elements (P) and (P ') while flowing through the adjacent passages (A) and (B), and the temperature thereof rises. At that time, the heat transfer plates (12) (14) constituting the heat transfer elements (P) (P ')
Since they are not in close contact with each other, their heat transfer coefficient is slightly inferior to that of a single sheet, but they do not significantly impair heat transfer performance as compared with a double partition wall in which a complete air layer is interposed. In addition, since the brazing (32) portion effectively acts on heat conduction, it is possible to secure a predetermined heat transfer performance.

漏れ等の試験を実施するに際しては、伝熱板(12)
(14)間の隙間(16)に一定流量の水を無圧で流し込
み、全量が抜け出るか否かを確かめればよい。なお、そ
のために注水口ないしヘッダーや排水受(いずれも図示
せず)を設けておくのが好ましい。
When conducting a leak test, the heat transfer plate (12)
It is sufficient to pour a constant flow rate of water into the gap (16) between the (14) without pressure and check whether all the water escapes. For that purpose, it is preferable to provide a water inlet, a header, and a drainage receiver (none of which are shown).

発明の効果 この発明によれば、所定の伝熱性能を確保しつつ、伝
熱板の腐食等による穴開きを確認して流体の漏れ、ない
しは混入を未然に防止しうる構造のプレート式熱交換器
を得ることができる。したがって、液質保証の見地から
この種の対策が義務付けられている分野におけるプレー
ト式熱交換器の実用化を可能にする上で著しい効果が認
められる。
EFFECTS OF THE INVENTION According to the present invention, a plate-type heat exchange having a structure capable of confirming perforation due to corrosion of a heat transfer plate and preventing fluid leakage or mixture while ensuring a predetermined heat transfer performance. You can get a vessel. Therefore, from the viewpoint of liquid quality assurance, a significant effect is recognized in enabling the practical application of the plate heat exchanger in the field where such measures are required.

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

第1図はこの発明の一実施例を模式的に示すプレート式
熱交換器の断面略図、 第2図A、Bは第1図のプレート式熱交換器の伝熱エレ
メントの正面略図であって、第2図Aは通路Aから見た
図、第2図Bは通路Bから見た図、 第3図は従来のプレート式熱交換器を説明するための略
図である。 P、P′:伝熱エレメント A、B:流体通路、 12、14:伝熱板、 16:隙間 32:ろう付け部。
FIG. 1 is a schematic sectional view of a plate heat exchanger schematically showing an embodiment of the present invention, and FIGS. 2A and 2B are schematic front views of heat transfer elements of the plate heat exchanger of FIG. 2A is a view as seen from a passage A, FIG. 2B is a view as seen from a passage B, and FIG. 3 is a schematic diagram for explaining a conventional plate heat exchanger. P, P ': Heat transfer element A, B: Fluid passage, 12, 14: Heat transfer plate, 16: Gap 32: Brazing part.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】伝熱エレメントを介して隣接する二系統の
流体通路内の流体相互間で熱交換が行われるものにおい
て、伝熱エレメントを一対の伝熱板で構成し、前記伝熱
板を水密でない程度の隙間を残して互いに接触させると
ともに外周で前記隙間を外部に開放させ、流体の出入口
となる貫通孔の周囲において水密に接合し、前記隙間と
連通させて注水口および排水受を設け、かつ、前記対の
伝熱板の伝熱部を互いに部分的にろう付けしたことを特
徴とするプレート式熱交換器。
1. A heat transfer element comprising a pair of heat transfer plates, wherein heat is exchanged between fluids in two fluid passages adjacent to each other via the heat transfer element. The gaps that are not watertight are left in contact with each other, and the gaps are opened to the outside at the outer periphery, and the gaps are watertightly joined around the through holes that serve as fluid inlets and outlets, and a water inlet and a drain receiver are provided in communication with the gaps. And a plate type heat exchanger in which the heat transfer portions of the pair of heat transfer plates are partially brazed to each other.
JP61299378A 1986-12-15 1986-12-15 Plate type heat exchanger Expired - Lifetime JPH0833286B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61299378A JPH0833286B2 (en) 1986-12-15 1986-12-15 Plate type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61299378A JPH0833286B2 (en) 1986-12-15 1986-12-15 Plate type heat exchanger

Publications (2)

Publication Number Publication Date
JPS63150591A JPS63150591A (en) 1988-06-23
JPH0833286B2 true JPH0833286B2 (en) 1996-03-29

Family

ID=17871788

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61299378A Expired - Lifetime JPH0833286B2 (en) 1986-12-15 1986-12-15 Plate type heat exchanger

Country Status (1)

Country Link
JP (1) JPH0833286B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4832958B2 (en) * 2006-05-23 2011-12-07 株式会社Lixil Bathtub apron connection structure
JP5095592B2 (en) * 2008-11-28 2012-12-12 株式会社日阪製作所 Heat transfer plate unit and plate type heat exchanger manufacturing method
SE533583C2 (en) * 2009-03-13 2010-10-26 Alfa Laval Corp Ab plate heat exchangers

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS621580Y2 (en) * 1981-01-23 1987-01-14

Also Published As

Publication number Publication date
JPS63150591A (en) 1988-06-23

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