JPH01256791A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPH01256791A JPH01256791A JP8381888A JP8381888A JPH01256791A JP H01256791 A JPH01256791 A JP H01256791A JP 8381888 A JP8381888 A JP 8381888A JP 8381888 A JP8381888 A JP 8381888A JP H01256791 A JPH01256791 A JP H01256791A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- pipe
- heat exchanger
- crack
- heat transmission
- 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.)
- Granted
Links
- 239000012530 fluid Substances 0.000 claims abstract description 11
- 229910052751 metal Inorganic materials 0.000 claims description 31
- 239000002184 metal Substances 0.000 claims description 31
- 238000001514 detection method Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 15
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052802 copper Inorganic materials 0.000 abstract description 3
- 239000010949 copper Substances 0.000 abstract description 3
- 230000005540 biological transmission Effects 0.000 abstract 5
- 239000002826 coolant Substances 0.000 description 15
- 238000010586 diagram Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】
[発明の目的コ
(産業上の利用分野)
本発明は、例えば高速増殖炉発電プラントの蒸気発生器
等に用いられるシェルアンドチューブ型の熱交換器に関
する。DETAILED DESCRIPTION OF THE INVENTION [Objective of the Invention (Field of Industrial Application) The present invention relates to a shell-and-tube heat exchanger used, for example, in a steam generator of a fast breeder reactor power plant.
(従来の技術)
高速増殖炉発電プラントに使用される蒸気発生器は、一
般に第4図に示すような構成となっている。すなわち、
図中41は中間部にベローズ42を介在させた竪型のシ
ェル容器で、このシェル容器41内の上部と下部には水
入口ブレナム43及び蒸気出口ブレナム44が設けられ
ている。(Prior Art) A steam generator used in a fast breeder reactor power plant generally has a configuration as shown in FIG. That is,
In the figure, reference numeral 41 denotes a vertical shell container with a bellows 42 interposed in the middle, and a water inlet blennium 43 and a steam outlet blemish 44 are provided at the upper and lower parts of the shell container 41.
これらの水入口ブレナム43及び蒸気出口ブレナム44
には、多数の伝熱管45・・・が上部管板46及び下部
管板47を貫通して開口しており、水流入口48より水
入口ブレナム43に流入した水は伝熱管45・・・内を
流通して蒸気出口ブレナム44に流出し、蒸気流出口4
9から図示しない蒸気配管を通りで発電タービンへ送ら
れるようになっている。また、シェル容器41の下側胴
部には二次冷却材流入口50が設けられ、この二次冷却
材流入口50より二次冷却材入口ブレナム51に流入し
た高温の二次冷却材(液体ナトリウム)は伝熱管45・
・・の外側を通って二次冷却材出口ブレナム52に流出
し、シェル容器41の上側胴部に設けられた二次冷却材
流出口53から図示しない二次冷却材戻り配管を通って
中間熱交換器へ戻るようになっている。These water inlet blennium 43 and steam outlet blennium 44
, a large number of heat exchanger tubes 45 are opened through the upper tube sheet 46 and the lower tube sheet 47, and the water flowing into the water inlet blennium 43 from the water inlet 48 flows into the heat exchanger tubes 45. flows through the steam outlet Blenheim 44, and flows out to the steam outlet Blenheim 44.
From 9, the steam is sent to the power generation turbine through a steam pipe (not shown). Further, a secondary coolant inlet 50 is provided in the lower body of the shell container 41, and high-temperature secondary coolant (liquid Sodium) is heat exchanger tube 45.
... flows out to the secondary coolant outlet blemish 52 through the outside of the shell container 41, and passes through the secondary coolant return pipe (not shown) from the secondary coolant outlet 53 provided in the upper body of the shell container 41 to the intermediate heat. It will now return to the exchanger.
また、このような蒸気発生器では伝熱管45・・・にク
ラック等が発生した場合、伝熱管45の内側を流通する
水(又は蒸気)と伝熱管45の外側を流通する二次冷却
材とが接触し、水・ナトリウム反応を起こすため、第5
図に示すように伝熱管45を内管54と外管55とから
なる二重管構造とし、伝熱管45の内側を流通する水(
又は蒸気)と伝熱管45の外側を流通する二次冷却材と
が接触しない構造となっている。また万が一1伝熱管4
5の内管54または外管55にクラック等が発生した場
合でもこれを早期に発見するために、上部管板46と下
部管板47との間に中間管板56を設け、この中間管板
56と下部管板57との間に形成された中間ブレナム5
8を通じてクラックの発生を検知できるようになってい
る。In addition, in such a steam generator, if a crack or the like occurs in the heat exchanger tubes 45, the water (or steam) flowing inside the heat exchanger tubes 45 and the secondary coolant flowing outside the heat exchanger tubes 45 will contact and cause a water-sodium reaction.
As shown in the figure, the heat exchanger tube 45 has a double tube structure consisting of an inner tube 54 and an outer tube 55, and the water flowing inside the heat exchanger tube 45 (
or steam) and the secondary coolant flowing outside the heat exchanger tubes 45 do not come into contact with each other. Also, in the unlikely event that heat transfer tube 4
In order to detect cracks early even if they occur in the inner tube 54 or outer tube 55 of 5, an intermediate tube sheet 56 is provided between the upper tube sheet 46 and the lower tube sheet 47. 56 and the lower tube plate 57
8, it is possible to detect the occurrence of cracks.
すなわち、伝熱管45の内管54にクラックが発生する
と、クラックの発生箇所から内管54内を流通する水(
又は蒸気)が漏洩し、内管54と外管55との間を通っ
て中間ブレナム58に流出するため、これをリーク検出
ノズル59に接続された漏洩検知機構(図示せず)で検
知するようになっている。また、伝熱管5の外管55に
クラックが発生した場合は、中間ブレナム58に封入さ
れたHe等の不活性ガスが外管55の外側に漏洩し、中
間ブレナム58内の圧力が低下するため、これを前記リ
ーク検出ノズル59に接続された圧力検知機構(図示せ
ず)で検出するようになっている。That is, when a crack occurs in the inner tube 54 of the heat transfer tube 45, water (
or steam) leaks and flows into the intermediate blemish 58 through the space between the inner pipe 54 and the outer pipe 55, so that this is detected by a leak detection mechanism (not shown) connected to the leak detection nozzle 59. It has become. Furthermore, if a crack occurs in the outer tube 55 of the heat transfer tube 5, the inert gas such as He sealed in the intermediate blemish 58 leaks to the outside of the outer tube 55, and the pressure inside the intermediate blemish 58 decreases. This is detected by a pressure detection mechanism (not shown) connected to the leak detection nozzle 59.
ところで、このような蒸気発生器では伝熱管45の内管
54と外管55との間に間隙部60が存在するため、伝
熱管45の伝熱性能が損われるという不具合がある。そ
こで、このような不具合を解決するために、第6図に示
す如く内管54と外管55との間に焼結金属等の多孔質
金属61を介在させ、伝熱管45の伝熱性能の低下を防
止した蒸気発生器が提案されている。しかしながら、こ
のような蒸気発生器は多孔質金属61の空隙率が伝熱管
45の軸方向及び周方向に均一でないため、クラックの
発生箇所によっては流体の漏洩を迅速に検知できなかっ
た。By the way, in such a steam generator, since the gap portion 60 exists between the inner tube 54 and the outer tube 55 of the heat exchanger tube 45, there is a problem that the heat transfer performance of the heat exchanger tube 45 is impaired. Therefore, in order to solve this problem, as shown in FIG. 6, a porous metal 61 such as sintered metal is interposed between the inner tube 54 and the outer tube 55 to improve the heat transfer performance of the heat transfer tube 45. A steam generator that prevents deterioration has been proposed. However, in such a steam generator, since the porosity of the porous metal 61 is not uniform in the axial direction and the circumferential direction of the heat transfer tube 45, fluid leakage cannot be quickly detected depending on the location where cracks occur.
(発明が解決しようとする課題)
このように伝熱管45の内管54と外管55との間に焼
結金属等の多孔質金属61を介在させた場合、伝熱管4
5の伝熱性能の低下を防止することはできるが、流体の
漏洩を迅速に検知できなくなるという問題があった。(Problem to be Solved by the Invention) When the porous metal 61 such as sintered metal is interposed between the inner tube 54 and the outer tube 55 of the heat exchanger tube 45 in this way, the heat exchanger tube 45
Although it is possible to prevent the deterioration of the heat transfer performance of No. 5, there is a problem that fluid leakage cannot be detected quickly.
本発明は、このような問題点に鑑みてなされたもので、
伝熱管の伝熱性能を損うことなく流体の漏洩を迅速に検
知できる熱交換器を提供しようとするものである。The present invention was made in view of these problems, and
The present invention aims to provide a heat exchanger that can quickly detect fluid leakage without impairing the heat transfer performance of heat exchanger tubes.
[発明の構成コ
(課題を解決するための手段)
上記の課題を解決するために本発明は、内管と外管とか
らなる伝熱管内を流通する流体の漏洩を上記内管と外管
との間隙を通じて検知する漏洩検知機構を備えた熱交換
器において、前記伝熱管の内管と外管との間に多数の金
属素線からなる金属編組体を設けたことを特徴とする。[Configuration of the Invention (Means for Solving the Problems) In order to solve the above problems, the present invention aims to prevent leakage of fluid flowing through a heat transfer tube consisting of an inner tube and an outer tube. The heat exchanger is equipped with a leakage detection mechanism that detects leakage through a gap between the heat exchanger tube and the heat exchanger tube, characterized in that a metal braided body made of a large number of metal wires is provided between the inner tube and the outer tube of the heat exchanger tube.
(作 用)
本発明では、伝熱管の内管と外管との間に多数の金属素
線からなる金属編組体を設けることにより、内管と外管
との間に流体通路が伝熱管の軸方向及び周方向に均一に
形成されるため、伝熱管の伝熱性能を損うことなく流体
の漏洩を迅速に検知することができる。(Function) In the present invention, by providing a metal braided body made of a large number of metal wires between the inner tube and the outer tube of the heat exchanger tube, a fluid passage is formed between the inner tube and the outer tube of the heat exchanger tube. Since they are formed uniformly in the axial and circumferential directions, fluid leakage can be quickly detected without impairing the heat transfer performance of the heat transfer tube.
(実施例) 以下、本発明の実施例を図面を参照して説明する。(Example) Embodiments of the present invention will be described below with reference to the drawings.
第1図は本発明に係る熱交換器を高速増殖炉発電プラン
トの蒸気発生器に適用した一実施例を示す断面図である
。同図において図中1は中間部にベローズ2を介在させ
た竪型のシェル容器で、このシェル容器1の内部には多
数の伝熱管3・・・が収納されている。これらの伝熱管
3・・・は第2図に示すように内管4と外管5とからな
り、内管4は上部管板6及び下部管板7を貫通してシェ
ル容器1内の上部と下部に形成された水入口ブレナム8
及び蒸気出口ブレナム9に開口している。FIG. 1 is a sectional view showing an embodiment in which a heat exchanger according to the present invention is applied to a steam generator of a fast breeder reactor power plant. In the figure, reference numeral 1 denotes a vertical shell container with a bellows 2 interposed in the middle, and a large number of heat exchanger tubes 3 are housed inside the shell container 1. These heat transfer tubes 3... consist of an inner tube 4 and an outer tube 5 as shown in FIG. and water inlet Blenheim 8 formed at the bottom.
and open to the steam outlet blennium 9.
上記水入口ブレナム8及び蒸気出口ブレナム9にはそれ
ぞれ水流入口10及び蒸気流出口11が設けられ、水流
入口10より水入口ブレナム8に流入した水は、伝熱管
3の内側つまり内管4内を通って蒸気出口ブレナム9に
流出し、蒸気流出口11より図示しない蒸気配管を通っ
て発電タービンへ送られるようになっている。A water inlet 10 and a steam outlet 11 are provided in the water inlet blennium 8 and steam outlet blennium 9, respectively. The steam flows through the steam outlet blenum 9, and is sent from the steam outlet 11 to the power generation turbine through a steam pipe (not shown).
また、前記シェル容器1の下側胴部には二次冷却材流入
口12が設けられ、この二次冷却材流入口12より二次
冷却材入口ブレナム13に流入した高温の二次冷却材(
液体ナトリウム)は、伝熱管3の外側つまり外管5の外
側を通って二次冷却材出口ブレナム14に流出し、シェ
ル容器1の上側胴部に設けられた二次冷却材流出口15
より図示しない二次冷却材戻り配管を通って中間熱交換
器へ戻るようになっている。Further, a secondary coolant inlet 12 is provided in the lower body of the shell container 1, and high temperature secondary coolant (
The liquid sodium) passes through the outside of the heat transfer tube 3, that is, the outside of the outer tube 5, and flows out into the secondary coolant outlet brenum 14, and then flows into the secondary coolant outlet 15 provided in the upper body of the shell container 1.
The coolant returns to the intermediate heat exchanger through a secondary coolant return pipe (not shown).
一方、前記上部管板6と下部管板7との間には中間管板
16.17が設けられ、これらの中間管板16.17と
上部管板6及び下部管板7との間には、それぞれ中間ブ
レナム18.19が形成されている。これらの中間ブレ
ナム18.19内にはHe等の不活性ガスが封入され、
伝熱管3の外管5を介して互いに連通している。また、
中間ブレナム18.19にはリーク検出ノズル20゜2
1が設けられ、これらのリーク検出ノズル20゜21に
はそれぞれ図示しない漏洩検知機構及び圧力検知機構が
接続されている。On the other hand, an intermediate tube sheet 16.17 is provided between the upper tube sheet 6 and the lower tube sheet 7, and between these intermediate tube sheets 16.17 and the upper tube sheet 6 and the lower tube sheet 7, , respectively, are formed with intermediate brenums 18,19. Inert gas such as He is sealed in these intermediate blemishes 18 and 19,
They communicate with each other via the outer tube 5 of the heat transfer tube 3. Also,
Leak detection nozzle 20゜2 is installed in the middle blemish 18.19.
1 are provided, and a leak detection mechanism and a pressure detection mechanism (not shown) are connected to these leak detection nozzles 20 and 21, respectively.
前記伝熱管3の内管4と外管5との間には、第2図に示
すように多数の金属素線からなる金属編組体22が設け
られている。この金属編組体22は、例えば第3図に示
すように銅等の複数本の金属素線を帯状に束ねた一対の
帯状体23a。As shown in FIG. 2, a metal braided body 22 made of a large number of metal wires is provided between the inner tube 4 and the outer tube 5 of the heat transfer tube 3. As shown in FIG. The metal braided body 22 is, for example, a pair of band-shaped bodies 23a made by bundling a plurality of metal wires such as copper into a band-like shape, as shown in FIG.
23bを網状に交互に編組したもので、内管4の外周面
と外管5の内周面に密接している。23b are alternately braided in a net shape, and are in close contact with the outer circumferential surface of the inner tube 4 and the inner circumferential surface of the outer tube 5.
上記のような構成において、例えば伝熱管3の内管4に
クラックが発生すると、内管4内を流通する水(又は蒸
気)がクラックの発生箇所から漏洩し、内管4と外管5
との間を通って中間ブレナム18.19に流出するため
、これをリーク検出ノズル20.21に接続された漏洩
検知機構で検知することによりクラックの発生を検知す
ることができる。In the above configuration, for example, if a crack occurs in the inner tube 4 of the heat transfer tube 3, the water (or steam) flowing inside the inner tube 4 leaks from the crack occurrence point, causing the inner tube 4 and the outer tube 5 to leak.
Since the leakage gas flows out into the intermediate blemish 18.19 through the gap between the leakage detection nozzle 20.21 and the leakage detection mechanism connected to the leakage detection nozzle 20.21, the occurrence of cracks can be detected.
また、伝熱管3の外管5にクラックが発生した場合は、
中間ブレナム18.19内に封入されたHe等の不活性
ガスがクラックの発生箇所から外管5の外側に漏洩し、
中間ブレナム18.19内の圧力が低下するため、これ
をリーク検出ノズル20.21に接続された圧力検知機
構で検知することによりクラックの発生を検知すること
ができる。In addition, if a crack occurs in the outer tube 5 of the heat exchanger tube 3,
An inert gas such as He sealed in the intermediate blemish 18, 19 leaks to the outside of the outer tube 5 from the crack occurrence location,
Since the pressure within the intermediate blemish 18.19 decreases, the occurrence of cracks can be detected by detecting this with a pressure sensing mechanism connected to the leak detection nozzle 20.21.
このように、伝熱管3の内管4と外管5との間に多数の
金属素線からなる金属編組体22を設けることにより、
内管4と外管5との間に流体通路が伝熱管3の軸方向及
び周方向に均一に形成されるため、伝熱管3の伝熱性能
を損うことなく流体の漏洩を迅速に検知することができ
る。また、金属編組体22は軸方向に縮めると径が大き
くなり、軸方向に伸ばすと径が小さくなるので、内管4
の外周に容易に挿入できるとともに、内管4の外周に均
一に密着させることができる。In this way, by providing the metal braided body 22 made of a large number of metal wires between the inner tube 4 and the outer tube 5 of the heat exchanger tube 3,
Since fluid passages are formed uniformly in the axial and circumferential directions of the heat transfer tubes 3 between the inner tube 4 and the outer tube 5, fluid leakage can be quickly detected without impairing the heat transfer performance of the heat transfer tubes 3. can do. Furthermore, when the metal braided body 22 is contracted in the axial direction, the diameter increases, and when stretched in the axial direction, the diameter decreases, so the inner tube 4
It can be easily inserted into the outer periphery of the inner tube 4, and it can be made to adhere uniformly to the outer periphery of the inner tube 4.
なお、本発明は上記実施例に限定されるものではない。Note that the present invention is not limited to the above embodiments.
例えば、金属編組体22を異種類の金属素線(例えば銅
とステンレス鋼等)で構成してもよい。このように金属
編組体22を異種類の金属素線で構成することにより、
金属編組体22の強度を高めることができる。さらに、
金属編組体22の表面にメツキを施すことにより、金属
編組体22の伝熱性能が向上するため、二次冷却拐の熱
を伝熱管3内を流通する水に効率よく伝えることができ
る。なお、金属編組体22は第3図に示したものに限定
されるものではなく、例えば多数の金属素線を網状に編
んだものでもよい。For example, the metal braided body 22 may be composed of different types of metal wires (eg, copper, stainless steel, etc.). By configuring the metal braided body 22 with different types of metal wires in this way,
The strength of the metal braided body 22 can be increased. moreover,
By plating the surface of the metal braided body 22, the heat transfer performance of the metal braided body 22 is improved, so that the heat of the secondary cooling can be efficiently transferred to the water flowing in the heat transfer tube 3. Note that the metal braided body 22 is not limited to that shown in FIG. 3, and may be one in which a large number of metal wires are knitted into a net shape, for example.
また、上記実施例では高速増殖炉発電プラントの蒸気発
生器について説明したが、本発明は一般の熱交換器にも
適用可能である。Furthermore, although the above embodiments have been described with respect to a steam generator for a fast breeder reactor power plant, the present invention is also applicable to general heat exchangers.
[発明の効果]
以上説明したように本発明によれば、伝熱管の伝熱性能
を損うことなく流体の漏洩を迅速に検知することができ
、熱交換器の信頼性を向上させることができる。[Effects of the Invention] As explained above, according to the present invention, fluid leakage can be quickly detected without impairing the heat transfer performance of the heat exchanger tubes, and the reliability of the heat exchanger can be improved. can.
第1図ないし第3図は本発明の一実施例を木す図で、第
1図は蒸気発生器の断面図、第2図は伝熱管の断面図、
第3図は金属編組体の一例を示す図である。また、第4
図ないし第6図は従来技術を説明するための図で、第4
図は蒸気発生器の断面図、第5図は伝熱管の断面図、第
6図は伝熱管の内管と外管との間に多孔質金属を介在さ
せた従来例を示す図である。
1・・・シェル容器、3・・・伝熱管、4・・・内管、
5・・・外管、10・・・水流入口、11・・・蒸気流
出口、12・・・二次冷却材流入口、15・・・二次冷
却材流出口、18.19・・・中間ブレナム、20.2
1・・・リーク検出ノズル、22・・・金属編組体。
出願人代理人 弁理士 鈴江武彦
第1図
第2図
第3図
第4図
第5図 第6図1 to 3 are wooden diagrams of an embodiment of the present invention, in which FIG. 1 is a sectional view of a steam generator, FIG. 2 is a sectional view of a heat exchanger tube,
FIG. 3 is a diagram showing an example of a metal braided body. Also, the fourth
Figures 6 through 6 are diagrams for explaining the prior art.
5 is a sectional view of a steam generator, FIG. 5 is a sectional view of a heat exchanger tube, and FIG. 6 is a diagram showing a conventional example in which a porous metal is interposed between an inner tube and an outer tube of a heat exchanger tube. 1... Shell container, 3... Heat exchanger tube, 4... Inner tube,
5... Outer pipe, 10... Water inlet, 11... Steam outlet, 12... Secondary coolant inlet, 15... Secondary coolant outlet, 18.19... Intermediate Blenheim, 20.2
1... Leak detection nozzle, 22... Metal braided body. Applicant's Representative Patent Attorney Takehiko Suzue Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 6
Claims (1)
上記内管と外管との間隙を通じて検知する漏洩検知手段
を備えた熱交換器において、前記伝熱管の内管と外管と
の間に多数の金属素線からなる金属編組体を設けたこと
を特徴とする熱交換器。In a heat exchanger equipped with a leakage detection means for detecting leakage of a fluid flowing through a heat exchanger tube consisting of an inner tube and an outer tube through a gap between the inner tube and the outer tube, the inner tube and the outer tube of the heat exchanger tube are A heat exchanger characterized in that a metal braided body made of a large number of metal wires is provided between the heat exchanger and the metal wire.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63083818A JPH0823476B2 (en) | 1988-04-05 | 1988-04-05 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63083818A JPH0823476B2 (en) | 1988-04-05 | 1988-04-05 | Heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01256791A true JPH01256791A (en) | 1989-10-13 |
JPH0823476B2 JPH0823476B2 (en) | 1996-03-06 |
Family
ID=13813266
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63083818A Expired - Lifetime JPH0823476B2 (en) | 1988-04-05 | 1988-04-05 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0823476B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7326811B2 (en) | 2001-09-28 | 2008-02-05 | Nippon Shokubai Co., Ltd. | Method for production of (meth)acrylic acid by use of a shell-and-tube heat exchanger |
CN106969515A (en) * | 2017-04-17 | 2017-07-21 | 山西泰杰地能干热岩有限公司 | The tree-shaped multiple spot heat exchange utilization system of ground energy hot dry rock and Application way |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63311091A (en) * | 1987-06-15 | 1988-12-19 | Babcock Hitachi Kk | Double thermal transmitting pipe for heat exchanger |
-
1988
- 1988-04-05 JP JP63083818A patent/JPH0823476B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63311091A (en) * | 1987-06-15 | 1988-12-19 | Babcock Hitachi Kk | Double thermal transmitting pipe for heat exchanger |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7326811B2 (en) | 2001-09-28 | 2008-02-05 | Nippon Shokubai Co., Ltd. | Method for production of (meth)acrylic acid by use of a shell-and-tube heat exchanger |
CN106969515A (en) * | 2017-04-17 | 2017-07-21 | 山西泰杰地能干热岩有限公司 | The tree-shaped multiple spot heat exchange utilization system of ground energy hot dry rock and Application way |
CN106969515B (en) * | 2017-04-17 | 2023-05-23 | 山西泰杰地能干热岩有限公司 | Geothermal energy dry-heat rock tree-shaped multipoint heat exchange comprehensive utilization system and utilization method |
Also Published As
Publication number | Publication date |
---|---|
JPH0823476B2 (en) | 1996-03-06 |
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