JPH03137534A - Heat transfer pipe and leak detecting system using this pipe - Google Patents

Heat transfer pipe and leak detecting system using this pipe

Info

Publication number
JPH03137534A
JPH03137534A JP1275581A JP27558189A JPH03137534A JP H03137534 A JPH03137534 A JP H03137534A JP 1275581 A JP1275581 A JP 1275581A JP 27558189 A JP27558189 A JP 27558189A JP H03137534 A JPH03137534 A JP H03137534A
Authority
JP
Japan
Prior art keywords
pipe
groove
tube
close contact
heat exchanger
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
JP1275581A
Other languages
Japanese (ja)
Inventor
Shinji Hatsutori
服部 進司
Umeo Inoue
梅夫 井上
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.)
Takuma Co Ltd
Original Assignee
Takuma Co 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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP1275581A priority Critical patent/JPH03137534A/en
Publication of JPH03137534A publication Critical patent/JPH03137534A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To detect a leak quickly by disposing an outer pipe in close contact with the outer peripheral surface of an inner pipe, by making a helical groove throughout a full length of the close contact part and by providing the opposite ends of the outer pipe with leak detecting holes communicating with the groove. CONSTITUTION:One or a plurality of helical grooves 4 are formed in the outer peripheral surface of a cylindrical smooth pipe of an inner pipe 2 throughout a full length of the pipe substantially. The part of the inner pipe 2 wherein the groove 4 is formed bulges inward to increase a heat transfer area, and thereby a rate of transfer of heat of a fluid in the pipe can be increased to 1.5 to 2.0 times higher than in an ordinary smooth pipe. An outer pipe 3 is a smooth pipe and it is fitted in a shrinkage on the outer peripheral surface of the inner pipe 2 and brought into close contact therewith by bulging or the like. The opposite ends of the outer pipe 3 and the outer peripheral surface of the inner pipe are sealed with each other as required. Moreover, leak detecting holes 5 communicating with the groove 4 are made in the opposite ends of the outer pipe 3. When a leak occurs from the pipe 2 or 3 or between the two pipes, the fluid permeates through an interface and runs into the groove 4 when the leak occurs in the close contact part of the two pipes, while the fluid runs immediately into the groove 4 when the leak occurs in the part of the groove 4. Accordingly, the leak can be detected from the detecting holes 5 quickly and easily even when it is caused by a very small damage.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、主に熱交換器等に用いられる伝熱管及びこれ
を用いた漏洩検知システムに関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a heat exchanger tube mainly used in a heat exchanger, etc., and a leakage detection system using the same.

(従来の技術) 第9図は従来から一般的に使用されている熱交換器の概
略断面図であって、当該熱交換器は、ダクト24に介設
したケーシング25内に多数の伝熱管26を配置して成
り、ダクト24内を流れる高温(低温)の気体Aと伝熱
管26内を流れる低温(高温)の液体Bとの間で熱交換
を行なうように為されている。
(Prior Art) FIG. 9 is a schematic cross-sectional view of a heat exchanger that has been commonly used. are arranged so that heat exchange is performed between the high temperature (low temperature) gas A flowing in the duct 24 and the low temperature (high temperature) liquid B flowing in the heat transfer tube 26.

尚、図に於いて、27は液体入口、28は入口八ッダー
、29は液体出口、3oは出口ヘッダ−31はスリーブ
、32はカバーである。
In the figure, 27 is a liquid inlet, 28 is an inlet header, 29 is a liquid outlet, 3o is an outlet header, 31 is a sleeve, and 32 is a cover.

(発明が解決しようとする課題) ところで、伝熱管26を有する従来の熱交換器は、不可
避的に生じる伝熱管26の損傷による漏洩が生じた場合
に異なる二つの流体A、Bが混合して様々な弊害を招く
ことがあった。
(Problems to be Solved by the Invention) By the way, in the conventional heat exchanger having the heat exchanger tubes 26, when leakage occurs due to the inevitable damage to the heat exchanger tubes 26, two different fluids A and B are mixed. This could lead to various negative effects.

即ち、気体A中に液体Bが混入することによって気体へ
の清浄性が損なわれたり、気体Aと液体Bが反応して有
害な作用を生じたり、液体Bが失われることによって液
体系統に障害が生じたり、或いは気体Aと液体Bの圧力
バランスが崩れて有害な作用を生じたりする等、様々な
弊害を招いていた。
In other words, mixing of liquid B into gas A may impair the cleanliness of the gas, gas A and liquid B may react to cause harmful effects, or loss of liquid B may cause damage to the liquid system. This has led to various problems, such as the occurrence of gas A and liquid B, or the pressure balance between gas A and liquid B being disrupted, resulting in harmful effects.

これらの弊害を無くすには伝熱管26のグレードを上げ
て伝熱管26に損傷が生じないようにするか、或いは伝
熱管26の溶接部(接合部)を両流体A、Bが接しない
ケーシング25外に配置する等の対策が通常行われてい
る。
In order to eliminate these problems, the grade of the heat exchanger tube 26 should be increased to prevent damage to the heat exchanger tube 26, or the welded part (joint part) of the heat exchanger tube 26 should be made of a casing 25 where both fluids A and B do not come in contact with each other. Measures such as placing it outside are usually taken.

然し乍ら、流体による伝熱管26の腐食、熱応力や繰り
返し応力による亀裂、膨張・収縮・振動による部品同志
の摩耗等によって生じる伝熱管26の損傷を皆無とする
ことは事実上困難であった。
However, it has been practically difficult to completely eliminate damage to the heat exchanger tubes 26 caused by corrosion of the heat exchanger tubes 26 due to fluids, cracks due to thermal stress and repeated stress, wear of parts together due to expansion, contraction, and vibration, and the like.

本発明は、このような実情に鑑み、損傷によって漏洩が
生じた場合に管内外を流れる流体が混合する前に漏洩を
速やかに検知し得る伝熱管及びこれを用いた漏洩検知シ
ステムを提供するにある。
In view of these circumstances, the present invention provides a heat exchanger tube and a leakage detection system using the same, which can quickly detect the leakage before the fluid flowing inside and outside the tube mixes when a leakage occurs due to damage. be.

(課題を解決する為の手段、) 上記目的を達成する為に、本発明の伝熱管は、内管の外
周面に外管を密接状態で配設し、両管の密接部に全長に
亘って螺旋状の溝を形成し、前記外管の両端部に溝に連
通ずる漏洩検知孔を夫々形成したものである。
(Means for Solving the Problems) In order to achieve the above object, the heat exchanger tube of the present invention has an outer tube disposed in close contact with the outer peripheral surface of the inner tube, and a heat exchanger tube that extends over the entire length in the close contact portion of both tubes. A spiral groove is formed in the outer tube, and leak detection holes communicating with the groove are formed at both ends of the outer tube.

又、漏洩検知システムは、内管の外周面に外管を密接状
態で配設し1両管の密接部に全長に亘って螺旋状の溝を
形成し、前記外管の両端部に溝に連通ずる漏洩検知孔を
夫々形成した伝熱管と、伝熱管の溝内にパージ用流体を
流すポンプ若しくは真空ポンプと、溝内を通過したパー
ジ用流体を検査する漏洩検知装置とから構成したもので
ある。
In addition, the leakage detection system has an outer tube disposed in close contact with the outer peripheral surface of the inner tube, a spiral groove is formed over the entire length in the close contact part of the two tubes, and a groove is formed at both ends of the outer tube. It consists of a heat transfer tube each having a communicating leak detection hole, a pump or vacuum pump that flows purge fluid into the groove of the heat transfer tube, and a leak detection device that inspects the purge fluid that has passed through the groove. be.

更に、他の漏洩検知システムは、内管の外周面に外管を
密接状態で配設し、両管の密接部に全長に亘って螺旋状
の溝を形成し、前記外管の両端部に溝に連通ずる漏洩検
知孔を夫々形成し、溝内を真空若しくは減圧状態に保っ
た伝熱管と、伝熱管の漏洩検知孔に接続された圧力計若
しくは圧力スイッチとから構成したものである。
Furthermore, other leakage detection systems have an outer tube disposed in close contact with the outer peripheral surface of the inner tube, a spiral groove is formed over the entire length in the close contact part of both tubes, and a spiral groove is formed at both ends of the outer tube. It consists of a heat exchanger tube, each having a leak detection hole communicating with the groove and keeping the inside of the groove in a vacuum or reduced pressure state, and a pressure gauge or pressure switch connected to the leak detection hole of the heat exchanger tube.

(作用) 伝熱管の内・外管に損傷が生じて流体が漏洩すると、こ
の流体は両管の密接部に形成した溝内に流入する。溝内
への流体の流入は、伝熱管の端部に形成した漏洩検知孔
から容易に検知することができる。
(Function) When damage occurs to the inner and outer tubes of the heat transfer tube and fluid leaks, this fluid flows into the groove formed in the close contact portion of both tubes. The inflow of fluid into the groove can be easily detected through a leakage detection hole formed at the end of the heat transfer tube.

即ち、伝熱管の溝内にパージ用流体を流し、漏洩検知孔
から排出されたパージ用流体を漏洩検知装置によって検
査した場合には流体の漏洩を速やかに検知することがで
きる。
That is, when the purge fluid is flowed into the groove of the heat transfer tube and the purge fluid discharged from the leakage detection hole is inspected by the leakage detection device, fluid leakage can be quickly detected.

又、伝熱管の溝内を真空若しくは減圧状態に保ち、漏洩
検知孔に圧力計や圧力スイッチ等を接続した場合には、
溝内の圧力変化によって流体の漏洩を速やかに検知する
ことができる。
In addition, if the inside of the heat transfer tube groove is kept in a vacuum or reduced pressure state and a pressure gauge or pressure switch is connected to the leakage detection hole,
Fluid leakage can be quickly detected by pressure changes within the groove.

(実施例) 以下、本発明の実施例を図面に基づいて詳細に説明する
(Example) Hereinafter, an example of the present invention will be described in detail based on the drawings.

第1図及び第2図は本発明の実施例に係る伝熱管lの断
面図であって、当該伝熱管1は内管2とこれの外周面に
密接状態で配設された外管3とから成り、両管2,3の
密接部には全長に亘って螺旋状の溝4が形成されている
1 and 2 are cross-sectional views of a heat exchanger tube l according to an embodiment of the present invention, in which the heat exchanger tube 1 includes an inner tube 2 and an outer tube 3 disposed in close contact with the outer peripheral surface of the inner tube 2. A spiral groove 4 is formed over the entire length of the tubes 2 and 3 in close contact with each other.

即ち、内管2は、円筒状の平滑管の外周面に螺旋状の溝
4を形成して成り、この溝4は管の略全長に亘って一条
若しくは数条形成されている。
That is, the inner tube 2 is formed by forming a spiral groove 4 on the outer peripheral surface of a cylindrical smooth tube, and one or several grooves 4 are formed over substantially the entire length of the tube.

又、内管2は、溝4を形成した部分が内方へ膨出されて
伝熱面積が大きくなるように為されて居り、管内を流れ
る流体の熱伝達率を通常の平滑管の1.5〜2.0倍に
高めることができる。
In addition, the inner tube 2 is designed so that the portion where the groove 4 is formed is bulged inward to increase the heat transfer area, and the heat transfer coefficient of the fluid flowing inside the tube is 1. It can be increased by 5 to 2.0 times.

一方、外管3は、通常の平滑管から成り、内管2の外周
面に、焼ばめ、外管3の絞り加工、内管2のバルジ加工
等によって熱の伝達に悪影響のない程度の接触圧でもっ
て密接状態で配設されている。
On the other hand, the outer tube 3 is made of a normal smooth tube, and the outer circumferential surface of the inner tube 2 is shrink-fitted, the outer tube 3 is drawn, the inner tube 2 is bulged, etc. to the extent that heat transfer is not adversely affected. They are arranged in close contact with contact pressure.

又、外管3の両端と内管2の外周面との間は必要に応じ
てシール溶接等のシール加工によってシールされている
Moreover, the space between both ends of the outer tube 3 and the outer circumferential surface of the inner tube 2 is sealed by seal processing such as seal welding, if necessary.

更に、外管3の両端部には内管2の溝4に連通する漏洩
検知孔5が夫々形成されている。
Furthermore, leak detection holes 5 are formed at both ends of the outer tube 3, respectively, and communicate with the grooves 4 of the inner tube 2.

尚、内管2及び外管3の材質には、用途に応じて炭素鋼
、特殊鋼、銅、アルミニウム、ステンレス等が用いられ
て居り、種々の組合せで使用されている。
The materials used for the inner tube 2 and the outer tube 3 include carbon steel, special steel, copper, aluminum, stainless steel, etc., depending on the purpose, and are used in various combinations.

而して、前記伝熱管1は、主に熱交換器に用いられ、内
管2内と外管3外とを温度の異なる二つの流体が流れる
ことによって熱交換が行われる。
The heat transfer tube 1 is mainly used as a heat exchanger, and heat exchange is performed by two fluids having different temperatures flowing inside the inner tube 2 and outside the outer tube 3.

若し、内管2又は外管3若しくは両方の管2゜3に微細
な損傷が生じて流体が漏洩すると、漏洩した流体は漏洩
個所が両管2,3の密接部である場合には両管2,3の
界面を浸透して溝4内に流入し、又、漏洩個所が溝4部
分である場合には直ちに溝4内に流入する。この溝4は
管の略全長に亘って形成され、且つ管端には溝4に連通
ずる漏洩検知孔5を形成しているので、微細な損傷によ
る漏洩であっても漏洩検知孔5から迅速且つ容易に検知
することができる。
If fluid leaks due to minute damage to the inner tube 2, outer tube 3, or both tubes 2 and 3, the leaked fluid will leak from both tubes 2 and 3 if they are in close contact with each other. It penetrates the interface between the tubes 2 and 3 and flows into the groove 4, and if the leakage point is in the groove 4, it immediately flows into the groove 4. This groove 4 is formed over almost the entire length of the pipe, and a leak detection hole 5 that communicates with the groove 4 is formed at the end of the pipe, so even if there is a leak due to minute damage, it can be detected quickly from the leak detection hole 5. Moreover, it can be easily detected.

従って、前記伝熱管を使用した場合には例え漏洩が生じ
ても、伝熱管1の内外を流れる二つの流体が混合するま
でに対策を講じることが可能となり、流体の混合による
様々な弊害を未然に防止することができ、装置全体の安
全性や信頼性が向上することになる。
Therefore, when using the heat exchanger tube, even if a leak occurs, it is possible to take measures before the two fluids flowing inside and outside the heat exchanger tube 1 mix, and various adverse effects caused by mixing of fluids can be prevented. This will improve the safety and reliability of the entire device.

第3図は他の実施例に係る伝熱管lの断面図であって、
これは外管3の外周面に多数のフィン6を付けたもので
あり、管外側の伝熱面積が2〜15倍に増大したもので
ある。この伝熱管1も上記実施例の伝熱管1と同様に漏
洩を迅速且つ容易に検知することができる。
FIG. 3 is a cross-sectional view of a heat exchanger tube l according to another embodiment,
This has a large number of fins 6 attached to the outer peripheral surface of the outer tube 3, and the heat transfer area on the outside of the tube is increased by 2 to 15 times. Similar to the heat exchanger tube 1 of the above embodiment, this heat exchanger tube 1 can also detect leakage quickly and easily.

尚、上記実施例に於いては、内管2のみに溝4を形成し
たが、他の実施例に於いては、第4図に示す如く、外管
3の内周面に螺旋状の溝4を形成しても良く、或いは第
5図に示す如く、内管2の外周面と外管3の外周面との
両方に螺旋状の溝4を形成するようにしても良い。これ
らの伝熱管1も上記実施例の伝熱管1と同様に熱伝達率
が向上すると共に、流体の漏洩を迅速且つ容易に検知す
ることができる。
In the above embodiment, the groove 4 was formed only on the inner tube 2, but in other embodiments, a spiral groove was formed on the inner circumferential surface of the outer tube 3, as shown in FIG. Alternatively, as shown in FIG. 5, a spiral groove 4 may be formed on both the outer circumferential surface of the inner tube 2 and the outer circumferential surface of the outer tube 3. These heat exchanger tubes 1 also have improved heat transfer coefficients like the heat exchanger tubes 1 of the above embodiments, and can quickly and easily detect fluid leakage.

第6図は上記構造の伝熱管1を用いた漏洩検知システム
の概略系統図であって、これは伝熱管1の溝4内にポン
プ7若しくは真空ポンプ8によって空気等のパージ用流
体9(伝熱管1の内外を流れる流体と異なる種類の流体
)を流し、溝4内を通過したパージ用流体9を漏洩検知
器10等から成る漏洩検知装置11で検査することによ
って流体の漏洩を検知するものであり、流体の漏洩に対
しては、電極式、フロート式、静電容量式等の検知方法
により、又、気体の漏洩に対しては、各種気体検知器に
より夫々概存の技術で検知することができるようになっ
ている。
FIG. 6 is a schematic system diagram of a leakage detection system using the heat transfer tube 1 having the above structure. Fluid leakage is detected by flowing a different type of fluid from the fluid flowing inside and outside the heat tube 1 and inspecting the purge fluid 9 that has passed through the groove 4 with a leakage detection device 11 comprising a leakage detector 10 and the like. Fluid leaks are detected using electrode-type, float-type, capacitance-type, etc. detection methods, and gas leaks are detected using various gas detectors using existing techniques. It is now possible to do so.

この漏洩検知システムではパージにより速やかに漏洩を
検知できるので、流体の混合による様々な弊害を未然に
防止することができる。
Since this leakage detection system can quickly detect leakage by purging, it is possible to prevent various adverse effects caused by mixing of fluids.

尚、複数の伝熱管1を用いるときにはこれらを第6図に
一点鎖線で示す如く、配管12によって並列的に接続す
るようにしても良い、この場合にはポンプ7.8と漏洩
検知装置11とは単一で機能させることができる。
In addition, when using a plurality of heat exchanger tubes 1, these may be connected in parallel by piping 12 as shown by the dashed line in FIG. can function alone.

第7図は他の実施例に係る漏洩検知システムの概略系統
図であって、これは伝熱管1の溝4内を真空装置によっ
て真空若しくは減圧状態に保ち、一方の漏洩検知孔5を
閉塞して他方の漏洩検知孔5に圧力計13や圧力スイッ
チ14等を接続したものである。
FIG. 7 is a schematic diagram of a leakage detection system according to another embodiment, in which the inside of the groove 4 of the heat exchanger tube 1 is kept in a vacuum or reduced pressure state by a vacuum device, and one of the leakage detection holes 5 is closed. A pressure gauge 13, a pressure switch 14, etc. are connected to the other leak detection hole 5.

若し、内管2若しくは外管3に微細な損傷が生じて流体
が少しでも漏洩すると、溝4内の総容積は極めて小さい
ので、少しの漏洩によっても溝4内の圧力が速やかに上
昇し、これを圧力計13の目視又は計器による監視若し
くは圧力スイッチ14による感知によって速やかに流体
の漏洩を検知することができる。
If even a small amount of fluid leaks due to minute damage to the inner tube 2 or outer tube 3, the total volume within the groove 4 is extremely small, so even a small leak will cause the pressure within the groove 4 to rise quickly. The leakage of the fluid can be immediately detected by visually observing the pressure gauge 13 or monitoring it with a meter, or by sensing it with the pressure switch 14.

従って、流体の混合による弊害を未然に防止することが
できる。
Therefore, it is possible to prevent problems caused by mixing of fluids.

第8図は本発明の伝熱管1を用いた熱交換器の概略断面
図であって、15は伝熱管1の漏洩検知孔5に接続され
た配管、16はタンク、17はパージ用ポンプ、18は
漏洩検知器、19はケーシング、20はダクト、21は
入口へラダー、22は出口ヘッダー、23はカバーであ
る。
FIG. 8 is a schematic sectional view of a heat exchanger using the heat exchanger tube 1 of the present invention, in which 15 is a pipe connected to the leak detection hole 5 of the heat exchanger tube 1, 16 is a tank, 17 is a purge pump, 18 is a leak detector, 19 is a casing, 20 is a duct, 21 is a ladder to the inlet, 22 is an outlet header, and 23 is a cover.

この場合にも流体が少しでも漏洩すると、これを速やか
に検知することができ、流体が混合するまでに対策を講
じることができる。
Even in this case, if even a small amount of fluid leaks, this can be quickly detected and countermeasures can be taken before the fluids mix.

(発明の効果) 請求項1の伝熱管に於いては、内管の外周面に外管を密
接状態で配設し、両管の密接部に全長に亘って螺旋状の
溝を形成し、前記外管の両端部に溝に連通ずる漏洩検知
孔を夫々形成する構成とした為、管が損傷して流体が漏
洩すると、この流体は溝内に流入することになる。その
結果、これを漏洩検知孔から容易に検知することができ
る。即ち、溝並びに漏洩検知孔によって伝熱管の漏洩を
迅速且つ容易に検知することができ、伝熱管の内外を流
れる流体が混合する前に対策を講じることが可能となる
(Effects of the Invention) In the heat exchanger tube according to claim 1, the outer tube is disposed in close contact with the outer peripheral surface of the inner tube, and a spiral groove is formed over the entire length in the close contact portion of both tubes, Since leak detection holes communicating with the groove are formed at both ends of the outer tube, if the tube is damaged and fluid leaks, this fluid will flow into the groove. As a result, this can be easily detected from the leakage detection hole. That is, the grooves and the leakage detection holes can quickly and easily detect leakage in the heat exchanger tube, and it is possible to take countermeasures before the fluids flowing inside and outside the heat exchanger tube mix.

又、Ul請求項の漏洩検知システムに於いては、伝熱管
の溝内にポンプ等によってパージ用流体を流し、溝内を
通過したパージ用流体を漏洩検知装置で検査する構成と
した為、流体の漏洩をより一層速やかに検知することが
でき、流体の混合による弊害を未然に防止することがで
きる。その結果、装置全体の安全性、信頼性の向上を図
れる。
In addition, in the leak detection system of the U1 claim, the purge fluid is flowed into the groove of the heat transfer tube by a pump or the like, and the purge fluid that has passed through the groove is inspected by the leak detection device. leakage can be detected even more quickly, and harmful effects caused by mixing of fluids can be prevented. As a result, the safety and reliability of the entire device can be improved.

更に、請求項3の漏洩検知システムにあっては、伝熱管
の溝内を真空若しくは減圧状態に保ち、伝熱管の漏洩検
知孔に圧力計等を接続する構成とした為、流体の漏洩を
溝内の圧力変化によって速やかに検知することができ、
上記漏洩検知システムと同様の効果を奏し得る。
Furthermore, in the leak detection system of claim 3, the inside of the groove of the heat exchanger tube is maintained in a vacuum or reduced pressure state, and a pressure gauge or the like is connected to the leak detection hole of the heat exchanger tube, so that fluid leakage is detected in the groove. It can be quickly detected by the pressure change inside.
The same effects as the leakage detection system described above can be achieved.

このように、本発明の伝熱管及び漏洩検知システムは、
従来は流体の混合の可能性の為に使用できなかった場合
でも使用することができ、技術的、経済的効果は顕著で
ある。
In this way, the heat exchanger tube and leakage detection system of the present invention,
It can be used even in cases where it could not be used conventionally due to the possibility of mixing fluids, and the technical and economical effects are significant.

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

第1図は本発明の実施例に係る伝熱管の断面図、第2図
は第1図のn−n線断面図、第3図は他の実施例に係る
伝熱管の断面図、第4図及び第5図は更に他の実施例に
係る伝熱管の一部を示す概略断面図、第6図は本発明の
漏洩検知システムの概略系統図、第7図は他の実施例に
係る漏洩検知システムの概略系統図、第8図は本発明の
伝熱管を用いた熱交換器の概略断面図、第9図は従来の
伝熱管を用いた熱交換器の概略断面図である。 1は伝熱管、2は内管、3は外管、4は溝、5は漏洩検
知孔、7はポンプ、8は真空ポンプ、9はパージ用流体
、11は漏洩検知装置、13は圧力計、14は圧力スイ
ッチ。
FIG. 1 is a sectional view of a heat exchanger tube according to an embodiment of the present invention, FIG. 2 is a sectional view taken along line nn in FIG. 1, FIG. 3 is a sectional view of a heat exchanger tube according to another embodiment, 5 and 5 are schematic sectional views showing a part of a heat exchanger tube according to another embodiment, FIG. 6 is a schematic system diagram of a leak detection system of the present invention, and FIG. 7 is a leakage according to another embodiment. FIG. 8 is a schematic sectional view of a heat exchanger using heat exchanger tubes of the present invention, and FIG. 9 is a schematic sectional view of a heat exchanger using conventional heat exchanger tubes. 1 is a heat transfer tube, 2 is an inner tube, 3 is an outer tube, 4 is a groove, 5 is a leak detection hole, 7 is a pump, 8 is a vacuum pump, 9 is a purging fluid, 11 is a leak detection device, 13 is a pressure gauge , 14 is a pressure switch.

Claims (1)

【特許請求の範囲】 1、内管(2)の外周面に外管(3)を密接状態で配設
し、両管(2)、(3)の密接部に全長に亘って螺旋状
の溝(4)を形成し、前記外管(3)の両端部に溝(4
)に連通する漏洩検知孔(5)を夫々形成したことを特
徴とする伝熱管。 2、内管(2)の外周面に外管(3)を密接状態で配設
し、両管(2)、(3)の密接部に全長に亘って螺旋状
の溝(4)を形成し、前記外管(3)の両端部に溝(4
)に連通する漏洩検知孔(5)を夫々形成した伝熱管(
1)と、伝熱管(1)の溝(4)内にパージ用流体(9
)を流すポンプ(7)若しくは真空ポンプ(8)と、溝
(4)内を通過したパージ用流体(9)を検査する漏洩
検知装置(11)とから構成したことを特徴とする漏洩
検知システム。 3、内管(2)の外周面に外管(3)を密接状態で配設
し、両管(2)、(3)の密接部に全長に亘って螺旋状
の溝(4)を形成し、前記外管(3)の両端部に溝(4
)に連通する漏洩検知孔(5)を夫々形成し、溝(4)
内を真空若しくは減圧状態に保った伝熱管(1)と、伝
熱管(1)の漏洩検知孔(5)に接続された圧力計(1
3)若しくは圧力スイッチ(14)とから構成したこと
を特徴とする漏洩検知システム。
[Claims] 1. An outer tube (3) is disposed in close contact with the outer circumferential surface of the inner tube (2), and a spiral shape is provided over the entire length in the close contact portion of both tubes (2) and (3). A groove (4) is formed at both ends of the outer tube (3).
) A heat exchanger tube characterized in that a leakage detection hole (5) communicating with each other is formed respectively. 2. The outer tube (3) is placed in close contact with the outer peripheral surface of the inner tube (2), and a spiral groove (4) is formed over the entire length in the close contact area of both tubes (2) and (3). Grooves (4) are formed at both ends of the outer tube (3).
Heat exchanger tubes (
1) and purge fluid (9) in the groove (4) of the heat transfer tube (1).
) or a vacuum pump (8), and a leakage detection device (11) that inspects the purge fluid (9) that has passed through the groove (4). . 3. The outer tube (3) is placed in close contact with the outer peripheral surface of the inner tube (2), and a spiral groove (4) is formed over the entire length in the close contact area of both tubes (2) and (3). Grooves (4) are formed at both ends of the outer tube (3).
) are formed with leak detection holes (5) communicating with the grooves (4).
A heat exchanger tube (1) whose inside is kept in a vacuum or reduced pressure state, and a pressure gauge (1) connected to a leak detection hole (5) of the heat exchanger tube (1).
3) or a pressure switch (14).
JP1275581A 1989-10-23 1989-10-23 Heat transfer pipe and leak detecting system using this pipe Pending JPH03137534A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1275581A JPH03137534A (en) 1989-10-23 1989-10-23 Heat transfer pipe and leak detecting system using this pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1275581A JPH03137534A (en) 1989-10-23 1989-10-23 Heat transfer pipe and leak detecting system using this pipe

Publications (1)

Publication Number Publication Date
JPH03137534A true JPH03137534A (en) 1991-06-12

Family

ID=17557451

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1275581A Pending JPH03137534A (en) 1989-10-23 1989-10-23 Heat transfer pipe and leak detecting system using this pipe

Country Status (1)

Country Link
JP (1) JPH03137534A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005201444A (en) * 2004-01-05 2005-07-28 Samsung Electronics Co Ltd Contamination control device, contamination control system and contamination control method of clean room

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5233583A (en) * 1975-09-09 1977-03-14 Nippon Kokan Kk <Nkk> Method of detecting leakage in double-pipe type pipelines
JPS56122885U (en) * 1980-02-20 1981-09-18
JPS57120874U (en) * 1981-01-23 1982-07-27
JPS5839923A (en) * 1981-09-02 1983-03-08 Sumitomo Metal Ind Ltd Double-pipe
JPH01208601A (en) * 1988-02-13 1989-08-22 Power Reactor & Nuclear Fuel Dev Corp Double-pipe steam generator
JPH0277649U (en) * 1988-11-30 1990-06-14

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5233583A (en) * 1975-09-09 1977-03-14 Nippon Kokan Kk <Nkk> Method of detecting leakage in double-pipe type pipelines
JPS56122885U (en) * 1980-02-20 1981-09-18
JPS57120874U (en) * 1981-01-23 1982-07-27
JPS5839923A (en) * 1981-09-02 1983-03-08 Sumitomo Metal Ind Ltd Double-pipe
JPH01208601A (en) * 1988-02-13 1989-08-22 Power Reactor & Nuclear Fuel Dev Corp Double-pipe steam generator
JPH0277649U (en) * 1988-11-30 1990-06-14

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005201444A (en) * 2004-01-05 2005-07-28 Samsung Electronics Co Ltd Contamination control device, contamination control system and contamination control method of clean room

Similar Documents

Publication Publication Date Title
US4918975A (en) Method and apparatus for testing fluid-filled systems for leaks
US3655224A (en) Multi-ply bellows structure with fluid pervious spacer
EP3084332B1 (en) Tank for heating a liquid with tubing for heat exchange, and a method for manufacturing the latter
US5063787A (en) Venturi arrangement
JPH04213066A (en) Flowing-state sensor for detecting flowing state in pipe
US3465727A (en) Steam generator and method of making the same
US4192373A (en) Leak detection system for duplex tube heat exchangers
US5646352A (en) Method and apparatus for measuring a parameter of a multiphase flow
JPH03137534A (en) Heat transfer pipe and leak detecting system using this pipe
CN108981420A (en) A kind of bilayer sleeve heat-exchanger rig suitable for hazardous fluids medium
JPH0878242A (en) Double-tube cooler
US7159473B1 (en) Internal tube support for flow elements providing for tube expansion within the flow element shell
JP2015108442A (en) Trap
CN211234865U (en) Online leak detector
CN209296166U (en) A kind of small-bore pipeline temperature measuring equipment
US4181005A (en) Hydrogen detector
CN208254721U (en) A kind of cooler core leak spot detector
CN210603617U (en) Prevent leaking pipeline medium temperature-detecting device
JP2010261655A (en) Condenser cooling pipe leakage inspection device
JPH07218316A (en) Differential pressure type water level measuring device
JP2543658B2 (en) Leak detector for pipe joints
SU1260633A1 (en) Method of determining moment and location of leakage in pipeline
JPS63215932A (en) Leakage detector
CN220454345U (en) Exhaust gas heat exchange device
CN218819678U (en) High temperature resistant probe suitable for heat distribution pipeline leakage detection