JPH02309197A - Heat transfer pipe leakage surveying method for heat exchange device - Google Patents

Heat transfer pipe leakage surveying method for heat exchange device

Info

Publication number
JPH02309197A
JPH02309197A JP12871689A JP12871689A JPH02309197A JP H02309197 A JPH02309197 A JP H02309197A JP 12871689 A JP12871689 A JP 12871689A JP 12871689 A JP12871689 A JP 12871689A JP H02309197 A JPH02309197 A JP H02309197A
Authority
JP
Japan
Prior art keywords
heat exchanger
heat transfer
transfer pipe
tube
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.)
Pending
Application number
JP12871689A
Other languages
Japanese (ja)
Inventor
Hiroshi Itagaki
板垣 博
Takayuki Nagashima
孝幸 長嶋
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP12871689A priority Critical patent/JPH02309197A/en
Publication of JPH02309197A publication Critical patent/JPH02309197A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To enable specifying of a leaky heat transfer pipe by a method wherein when the leaky heat transfer pipe can not be specified visibly, sheets for detection are inserted from two directions symmetrical with respect to a piping row in a manner to contain the heat transfer pipe to be surveyed, and outflow water drops are confirmed. CONSTITUTION:When a heat transfer pipe 8d leaks, water drops are detected at the outer peripheral group of a pipe group. A specified number of sheets 20a for detection having size large enough to allow carriage of them through the manhole of an exhaust heat recovery heat exchanger from the upper part or the lower part of a pipe group is inserted along the alignment direction of the heat transfer pipe in the vicinity of a place where the water drops are detected. When the sheets 20a for detection are inserted in a manner to nip the heat transfer pipe 8d therebetween, water drops flowing out from the heat transfer pipe 8d flow along the sheets 20a for detection flows to a lower end. Water drops 21 are conformed, and after a row 22 of the heat transfer pipe is distinguished by means of a discriminating mark, the sheets 20a for detection are pulled off, and is inserted along alignment of the heat transfer pipe symmetrically to a preceding direction. This method enables the heat transfer pipe 8d being an intersection between two rows to be specified as a heat transfer, to which leakage occurs, basedon rows 22 and 23 of the heat transfer pipes on which the discriminating marks are drawn.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は、例えばコンバインドサイクル発電プラントに
用いられる排熱回収熱交換器における伝熱管の漏洩事故
の応急対策時に目視によってはその伝熱管を特定するの
が困麺な場合に適用される伝熱管漏洩探査方法に関する
[Detailed Description of the Invention] [Objective of the Invention] (Industrial Field of Application) The present invention provides a method for detecting a heat transfer tube leakage accident by visual inspection, for example, in an emergency measure against a heat transfer tube leakage accident in an exhaust heat recovery heat exchanger used in a combined cycle power generation plant. The present invention relates to a heat exchanger tube leakage detection method that is applied when it is difficult to identify the heat exchanger tube.

(従来の接緒) 従来の技術を第2図、第3図および第4図を用いて説明
する。
(Conventional Welding) A conventional technique will be explained using FIGS. 2, 3, and 4.

第2図はガスタービンと蒸気タービンとを組合せたコン
バインドサイクル発電プラントの概略系統を示す。
FIG. 2 shows a schematic system of a combined cycle power plant that combines a gas turbine and a steam turbine.

まず、空気圧縮機2によって吸い込まれた外気1は、こ
こで圧縮されて高圧となり、燃焼器3へ供給される。燃
焼器3では、さらに燃料が加えられ、燃焼して高温・高
圧の燃焼ガスとなって、ガスタービン4に送られる。ガ
スタービン4に導入された燃焼ガスは、ここで膨張して
仕事をし、図示しない羽根車を回転させ、発電機5を駆
動させる。ガスタービン4にて仕事をした燃焼ガスは、
膨張した排気ガスとなってダクト6を通り排熱回収ボイ
ラ7に導かれる。
First, outside air 1 sucked in by the air compressor 2 is compressed here, becomes high pressure, and is supplied to the combustor 3. In the combustor 3 , fuel is further added and combusted to become high-temperature, high-pressure combustion gas, which is sent to the gas turbine 4 . The combustion gas introduced into the gas turbine 4 expands and performs work, rotates an impeller (not shown), and drives the generator 5. The combustion gas that did work in the gas turbine 4 is
The expanded exhaust gas passes through the duct 6 and is guided to the exhaust heat recovery boiler 7.

この排気ガスの温度は通常500℃〜600℃と高温で
あり、この排気ガスをそのまま廃棄するのは大きな熱的
損失であり不経済である。このため、排熱回収熱交換器
7が設けられ、ここで排気ガス中に含まれる残留熱を回
収している。排熱回収熱交換器7に導入された排気ガス
は、伝熱管8内を通る給水と熱交換して冷却され、低温
のガスとなって煙突10から大気中に放出される。
The temperature of this exhaust gas is usually as high as 500° C. to 600° C., and it is uneconomical to dispose of this exhaust gas as it is due to a large thermal loss. For this reason, an exhaust heat recovery heat exchanger 7 is provided to recover residual heat contained in the exhaust gas. The exhaust gas introduced into the exhaust heat recovery heat exchanger 7 is cooled by exchanging heat with the water supply passing through the heat exchanger tubes 8, and is released into the atmosphere from the chimney 10 as a low-temperature gas.

次に、水、蒸気の流れに沿ってこのプラント構成を見る
Next, we will look at this plant configuration along the flow of water and steam.

蒸気タービン10に導入された蒸気は膨張して仕事をし
、膨張した蒸気は復水器11に排呂されて凝縮し、復水
となる。この復水は給水ポンプ12を備えた給水系統1
3を通り、排熱回収熱交換器7の節炭器14に送られ、
この節炭器14にて加熱される。
The steam introduced into the steam turbine 10 is expanded to perform work, and the expanded steam is exhausted to the condenser 11 and condensed to become condensed water. This condensate is supplied to a water supply system 1 equipped with a water supply pump 12.
3, and is sent to the energy saver 14 of the exhaust heat recovery heat exchanger 7.
It is heated by this economizer 14.

加熱された給水は蒸気ドラム15の下部水中に送り込ま
れる。
The heated feed water is fed into the water below the steam drum 15.

蒸気ドラム15内の水は、排卵ポンプ16により蒸発器
17に送られる。蒸発器17内を通る給水は加熱されて
順次蒸発し、気液二相流となって蒸気ドラム15の上部
蒸気中に戻され、気液に分離される。
Water in the steam drum 15 is sent to an evaporator 17 by an ovulation pump 16. The feed water passing through the evaporator 17 is heated and sequentially evaporated, becomes a gas-liquid two-phase flow, is returned to the upper steam of the steam drum 15, and is separated into gas and liquid.

蒸気ドラム15の上部に溜められた蒸気は、図示しない
湿分分離器を経て湿分分離された後、過熱器18に送ら
れ過熱蒸気となって蒸気タービン10に導入され、蒸気
タービン11を駆動させるようになっている。排熱回収
熱交換器7内に収容される節炭器14.蒸発器17.過
熱器18は、各々伝熱面積を大きくしたフィン付の伝熱
管8の群により構成されている。これらの管群は流体励
起振動による疲労破損を防ぐため適当な間隔で配置され
た支え板19で支持される。
The steam stored in the upper part of the steam drum 15 undergoes moisture separation through a moisture separator (not shown), and is then sent to the superheater 18 to become superheated steam, which is introduced into the steam turbine 10 to drive the steam turbine 11. It is designed to let you do so. A energy saver 14 housed in the exhaust heat recovery heat exchanger 7. Evaporator 17. The superheater 18 is composed of a group of finned heat transfer tubes 8 each having a large heat transfer area. These tube groups are supported by support plates 19 arranged at appropriate intervals to prevent fatigue failure due to fluid-induced vibration.

節炭器14.蒸発器17.過熱器18に使用される伝熱
管8を第3図に示す。
Economizer 14. Evaporator 17. A heat exchanger tube 8 used in the superheater 18 is shown in FIG.

伝熱管8の長さは普通熱交換性能を考慮して40〜50
mの長さが必要となる。伝熱管8を長くすることにより
、排熱回収熱交換器7の機器が長大となることを防ぐた
め、伝熱管8は蛇管状に形成され、伝熱管直管部の長さ
を10m前後にしている。
The length of the heat exchanger tube 8 is usually 40 to 50 mm in consideration of heat exchange performance.
A length of m is required. In order to prevent the equipment of the waste heat recovery heat exchanger 7 from becoming long by making the heat exchanger tubes 8 long, the heat exchanger tubes 8 are formed in a serpentine tube shape, and the length of the straight section of the heat exchanger tubes is approximately 10 m. There is.

このため伝熱管8は第3図に示す如くU字形伝熱管8a
と直管状伝熱管8bとを溶接接続し、所定の長さにして
いる。節炭器14.蒸発器17.過熱器18の管群は、
このような蛇行状伝熱管8が数百本より構成されており
、伝熱管8の管配列は第4図に示すように千鳥配列とす
るのが一般的である。
Therefore, the heat exchanger tube 8 has a U-shaped heat exchanger tube 8a as shown in FIG.
and a straight heat exchanger tube 8b are welded and connected to have a predetermined length. Economizer 14. Evaporator 17. The tube group of the superheater 18 is
Several hundred such meandering heat exchanger tubes 8 are constructed, and the tube arrangement of the heat exchanger tubes 8 is generally in a staggered arrangement as shown in FIG.

(発明が解決しようとする課題) 上述したような排熱回収熱交換器7において、運転中に
伝熱管8に漏洩事故が発生し、伝熱管8内の高温・高圧
の蒸気または水が管外に噴出することがある。伝熱管8
に漏洩が発生した場合、直ちに排熱回収熱交換器7の運
転を停止し、伝熱管8の漏洩部を特定し、漏洩した伝熱
管8を栓で塞いでしまう等の処置を取り、運転を再開す
る必要がある。第4図に示すような管配列においては。
(Problem to be Solved by the Invention) In the exhaust heat recovery heat exchanger 7 as described above, a leakage accident occurs in the heat exchanger tube 8 during operation, and high temperature and high pressure steam or water inside the heat exchanger tube 8 leaks outside the tube. may erupt. Heat exchanger tube 8
If a leak occurs, immediately stop the operation of the waste heat recovery heat exchanger 7, identify the leakage part of the heat exchanger tube 8, take measures such as plugging the leaked heat exchanger tube 8 with a plug, and then restart the operation. Need to restart. In a tube arrangement as shown in FIG.

伝熱管8の漏洩箇所が配管列の外周部の伝熱管8Cであ
れば、特定は容易であるが、管群の外周から内に入った
ところの伝熱管8dで漏洩が発生した場合は、その特定
が難しく、多大の時間を要することになる。このような
漏洩後の運転再開は緊急を要するのが普通であり、漏洩
部の探査は手際よく進めることが求められるが、充分に
応えることができない。
If the leakage point of the heat exchanger tube 8 is the heat exchanger tube 8C on the outer periphery of the pipe row, it is easy to identify, but if the leak occurs in the heat exchanger tube 8d that enters inside from the outer periphery of the tube group, it is difficult to identify the leakage point. Identification is difficult and takes a lot of time. Normally, resumption of operation after such a leak is urgent, and the search for the leakage part is required to proceed quickly, but this cannot be done satisfactorily.

そこで、本発明の目的は熱交換装置の伝熱管群の外周か
ら内に入ったところの伝熱管に漏洩が発生した場合に容
易に漏洩した伝熱管を特定することのできる熱交換装置
の伝熱管漏洩探査方法を提供することにある。
Therefore, an object of the present invention is to provide a heat exchanger tube for a heat exchanger that can easily identify the leaked heat exchanger tube when a leak occurs in a heat exchanger tube that enters from the outer periphery of a group of heat exchanger tubes in the heat exchanger. The object of the present invention is to provide a leakage detection method.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段) 本発明の特徴とするところは、千鳥に配置される多数の
伝熱管から構成される熱交換装置にて伝熱管の群の外周
部から内に入ったところのある伝熱管から内部流体が流
出したときの漏洩中の伝熱管を探査する方法であって、
検出用薄板を注目している伝熱管を含むように管配列に
沿って一定枚数挿入して検出用薄板の表面を伝わって流
れる内部流体から注目している伝熱管を含む一の列を特
定し、その後検出用薄板をそこから引抜き、先の挿入方
向と対称となる向きに注目している伝熱管を含むように
管配列に沿って挿入して検出用薄板の表面を伝わって流
れる内部流体から注目している伝熱管を含む他の列を特
定し、上記双方の伝熱管の列が交差する点に漏洩中の伝
熱管を見出すものである。
(Means for Solving the Problems) A feature of the present invention is that in a heat exchange device consisting of a large number of heat transfer tubes arranged in a staggered manner, A method for detecting a leaking heat exchanger tube when internal fluid flows out from a heat exchanger tube, the method comprising:
A certain number of detection thin plates are inserted along the tube array so as to include the heat transfer tube of interest, and one row containing the heat transfer tube of interest is identified from the internal fluid flowing along the surface of the detection thin plate. , the sensing thin plate is then pulled out from there and inserted along the tube array to include the heat transfer tubes in a direction symmetrical to the previous insertion direction to remove the internal fluid flowing along the surface of the sensing thin plate. The other row containing the heat exchanger tube of interest is specified, and the leaking heat exchanger tube is found at the point where both of the above-mentioned two rows of heat exchanger tubes intersect.

(作 用) 鍋交換装置の伝熱管群の外周部から入ったところの伝熱
管に漏洩が発生し、目視によってはその漏洩した伝熱管
を特定しないとき、検出用薄板を注目している伝熱管を
含むように管配列に沿って対称関係を保って2つの方向
から挿入し、双方の列を特定する。
(Function) When a leak occurs in a heat exchanger tube that enters from the outer periphery of a group of heat exchanger tubes in a pan exchanger, and the leaked heat exchanger tube cannot be identified by visual inspection, the heat exchanger tube that is focused on the thin detection plate are inserted from two directions in a symmetrical relationship along the tube arrangement so as to include both rows.

このとき、検出用薄板が対称関係にある限り、双方の列
の交差する点に漏洩の発生した伝熱管を見出すことがで
き、容易にその位置が特定される。
At this time, as long as the detection thin plates are symmetrical, the leaky heat exchanger tube can be found at the intersection of both rows, and its position can be easily identified.

したがって、緊急を要する熱交換装置の運転再開に寄与
するところが大きい。
Therefore, it greatly contributes to restarting the operation of the heat exchange device, which is required urgently.

(実施例) 以下、本発明の一実施例を示1図を参照して説明する。(Example) Hereinafter, one embodiment of the present invention will be described with reference to FIG.

なお、以下の説明は節炭器14.蒸発器17.過熱器1
8の管群の何れにも当てはめること°ができるが、便宜
上第4図にて示された伝熱管8dに漏洩が発生したもの
と仮定して説明されるものである。
Note that the following explanation is based on the economizer 14. Evaporator 17. Superheater 1
Although this can be applied to any of the tube groups 8, for convenience, the explanation will be based on the assumption that leakage has occurred in the heat exchanger tube 8d shown in FIG.

伝熱管8dに漏洩が発生した場合、伝熱管8d内の水が
破損部から管外に流出するため、管群外周部に水滴が見
出される。この水滴が見付けられた近傍の伝熱管の配列
方向に沿って管群の上部または下部より排熱回収熱交換
器のマンホールを通して搬入できる大きさの検出用薄板
20aを一定枚数挿入する。検出用薄板20aが伝熱管
8dを挟むように伝熱管と伝熱管との間に挿入されると
、伝熱管8dの破損部から流出する水滴は、検出用薄板
20aを伝わって下側へ流れ、その下端に達する。
When a leak occurs in the heat exchanger tube 8d, the water inside the heat exchanger tube 8d flows out of the tube from the broken part, so that water droplets are found on the outer periphery of the tube group. A certain number of detection thin plates 20a of a size that can be carried through the manhole of the exhaust heat recovery heat exchanger are inserted from the upper or lower part of the tube group along the arrangement direction of the heat exchanger tubes in the vicinity where the water droplets are found. When the detection thin plate 20a is inserted between the heat exchanger tubes so as to sandwich the heat exchanger tube 8d, water droplets flowing out from the broken part of the heat exchanger tube 8d flow downward through the detection thin plate 20a, Reach its lower end.

この検出用薄板20の下端に流れた水滴21を確認し、
伝熱管8dが含まれる伝熱管の列22を特定し、適当な
識別マークを用いて他の列と区別する。その後検出用薄
板20aを管群から引抜き、先の方向と対称となるよう
に伝熱管の配列に沿ってこれを挿入する。
Check the water droplets 21 that have flowed to the lower end of this detection thin plate 20,
The heat exchanger tube row 22 containing the heat exchanger tube 8d is identified and distinguished from other rows using an appropriate identification mark. Thereafter, the detection thin plate 20a is pulled out from the tube group and inserted along the arrangement of the heat exchanger tubes so as to be symmetrical to the previous direction.

上記と同様に伝熱管8dの破損部から流出する水滴を検
出用薄板20bの下端にて確認(水滴21)シ、伝熱管
8dの含まれる伝熱管の列23に識別マークを描く。識
別マークで他の列との区別が付いた後に検出用薄板20
bは管群から引抜く。
Similarly to the above, water droplets flowing out from the damaged portion of the heat exchanger tube 8d are confirmed at the lower end of the detection thin plate 20b (water droplets 21), and an identification mark is drawn on the row 23 of heat exchanger tubes in which the heat exchanger tube 8d is included. After the identification mark distinguishes it from other rows, the detection thin plate 20
b is pulled out from the tube group.

以上の手順で識別マークを描いた伝熱管の列22および
23に基づいて双方の交点にある伝熱管8dを漏洩が発
生した伝熱管であると特定する。
Based on the heat exchanger tube rows 22 and 23 on which identification marks have been drawn in accordance with the above procedure, the heat exchanger tube 8d located at the intersection of the two is identified as the heat exchanger tube in which the leak has occurred.

このように、管群外周から内に入ったところの伝熱管に
漏洩が発生しても、容易にその伝熱管を特定することが
でき、伝熱管を栓で塞いで水あるいは蒸気が流れ込まな
いように処置する。
In this way, even if a leak occurs in a heat exchanger tube that enters from the outer periphery of the tube group, it is easy to identify the heat exchanger tube, and the heat exchanger tube can be plugged with a plug to prevent water or steam from flowing in. be treated.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明は、千鳥に配置される多数の
伝熱管から構成される熱交換装置にて伝熱管の群の外周
部から内に入ったところのある伝熱管から内部流体が流
出したとき、検出用薄板を漏洩中の注目している伝熱管
を含むように管配列に沿って一定枚数挿入して検出用薄
板の表面を伝わって流れる内部流体から注目している伝
熱管を含む一の列を特定し、その後検出用薄板をそこか
ら引抜き、先の挿入方向と対称となる向きに注目してい
る伝熱管を含むように管配列に沿って挿入して検出用薄
板の表面を伝わって流れる内部流体から注目している伝
熱管を含む他の列を特定し、この双方の伝熱管の列が交
差する点に漏洩中の伝熱管を見出すようにしているから
、管群の外周部から内に入ったところの伝熱管に漏洩が
発生しても、容易にその伝熱管を特定することができ、
熱交換装置の運転再開が早期になし得るという優れた効
果を奏する。
As explained above, the present invention provides a heat exchange device consisting of a large number of heat exchanger tubes arranged in a staggered manner, in which internal fluid flows out from a certain heat exchanger tube that enters from the outer periphery of a group of heat exchanger tubes. When a certain number of detection thin plates are inserted along the tube array so as to include the leaking heat transfer tube of interest, the internal fluid flowing along the surface of the detection thin plate is removed from the one containing the heat transfer tube of interest. The detection thin plate is then pulled out from there, and the heat transfer is inserted along the tube array to include the focused heat transfer tube in a direction symmetrical to the previous insertion direction, so that the heat is transmitted along the surface of the detection thin plate. The system identifies the other row containing the heat exchanger tube of interest from the internal fluid flowing through it, and locates the leaking heat exchanger tube at the point where both rows of heat exchanger tubes intersect. Even if a leak occurs in a heat exchanger tube that has entered the inside of the pipe, the heat exchanger tube can be easily identified.
This provides an excellent effect in that the operation of the heat exchange device can be restarted quickly.

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

第1図は本発明による伝熱管漏洩探査方法を説明するた
めの図、第2図は従来のコンバインドサイクル発電プラ
ントを示す概略系統図、第3図は節炭器、蒸発器、過熱
器の伝熱管に使用されるフィン付伝熱管を示す構成図、
第4図は節炭器。 蒸発器、過熱器の伝熱管の管配列図である。 7・・・排熱回収熱交換器 8・・・伝熱管8a・・・
U字形伝熱管   8b・・・直管状伝熱管8c、 8
d・・・漏洩の生じた伝熱管14・・・節炭器    
  17・・・蒸発器18・・・過熱器      2
0a、 20b・・・検出用薄板21・・・水滴   
    22.23・・・伝熱管の列代理人 弁理士 
 則 近 憲 佑 同     第子丸   健 第1図 第 2 図 第3図
Fig. 1 is a diagram for explaining the heat transfer tube leakage detection method according to the present invention, Fig. 2 is a schematic system diagram showing a conventional combined cycle power plant, and Fig. 3 is a diagram for explaining the heat exchanger tube leakage detection method according to the present invention. A configuration diagram showing a finned heat exchanger tube used as a heat tube,
Figure 4 is a economizer. It is a tube arrangement diagram of heat exchanger tubes of an evaporator and a superheater. 7...Exhaust heat recovery heat exchanger 8...Heat transfer tube 8a...
U-shaped heat exchanger tube 8b...straight heat exchanger tube 8c, 8
d...Heat transfer tube 14 where leakage occurred...Economic device
17...Evaporator 18...Superheater 2
0a, 20b... thin plate for detection 21... water droplet
22.23...Heat transfer tube line agent Patent attorney
Nori Chika Ken Yudo Daishimaru Ken Figure 1 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 千鳥に配置される多数の伝熱管から構成される熱交換装
置にて前記伝熱管の群の外周部から内に入ったところの
ある伝熱管から内部流体が流出したときの漏洩中の伝熱
管を探査する方法であって、検出用薄板を注目している
伝熱管を含むように管配列に沿って一定枚数挿入して前
記検出用薄板の表面を伝わって流れる内部流体から注目
している伝熱管を含む一の列を特定し、その後前記検出
用薄板をそこから引抜き、先の挿入方向と対称となる向
きに注目している伝熱管を含むように管配列に沿って挿
入して前記検出用薄板の表面を伝わって流れる内部流体
から注目している伝熱管を含む他の列を特定し、上記双
方の伝熱管の列が交差する点に漏洩中の伝熱管を見出す
ことを特徴とする熱交換装置の伝熱管漏洩探査方法。
In a heat exchange device consisting of a large number of heat exchanger tubes arranged in a staggered manner, leaking heat exchanger tubes are detected when internal fluid flows out from a heat exchanger tube that enters from the outer periphery of a group of heat exchanger tubes. A method of detecting a heat exchanger tube by inserting a certain number of detection thin plates along a tube arrangement so as to include the heat transfer tube of interest from the internal fluid flowing along the surface of the detection thin plate. After that, the detection thin plate is pulled out from there, and the detection thin plate is inserted along the tube array so as to include the heat transfer tube whose orientation is symmetrical to the previous insertion direction. A heat exchanger characterized by identifying another row containing the heat exchanger tube of interest from the internal fluid flowing along the surface of the thin plate, and finding the leaking heat exchanger tube at the point where both of the above rows of heat exchanger tubes intersect. Method for detecting leakage in heat exchanger tubes of exchange equipment.
JP12871689A 1989-05-24 1989-05-24 Heat transfer pipe leakage surveying method for heat exchange device Pending JPH02309197A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12871689A JPH02309197A (en) 1989-05-24 1989-05-24 Heat transfer pipe leakage surveying method for heat exchange device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12871689A JPH02309197A (en) 1989-05-24 1989-05-24 Heat transfer pipe leakage surveying method for heat exchange device

Publications (1)

Publication Number Publication Date
JPH02309197A true JPH02309197A (en) 1990-12-25

Family

ID=14991663

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12871689A Pending JPH02309197A (en) 1989-05-24 1989-05-24 Heat transfer pipe leakage surveying method for heat exchange device

Country Status (1)

Country Link
JP (1) JPH02309197A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012202641A (en) * 2011-03-28 2012-10-22 Jfe Engineering Corp Gas heating system
JP2015219168A (en) * 2014-05-20 2015-12-07 株式会社東芝 Leakage detection apparatus and leakage detection method of heat exchanger

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012202641A (en) * 2011-03-28 2012-10-22 Jfe Engineering Corp Gas heating system
JP2015219168A (en) * 2014-05-20 2015-12-07 株式会社東芝 Leakage detection apparatus and leakage detection method of heat exchanger

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