JPS606443B2 - Heat shielding device for descending section of heat exchanger tube of liquid metal heating steam generator - Google Patents
Heat shielding device for descending section of heat exchanger tube of liquid metal heating steam generatorInfo
- Publication number
- JPS606443B2 JPS606443B2 JP13468077A JP13468077A JPS606443B2 JP S606443 B2 JPS606443 B2 JP S606443B2 JP 13468077 A JP13468077 A JP 13468077A JP 13468077 A JP13468077 A JP 13468077A JP S606443 B2 JPS606443 B2 JP S606443B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat exchanger
- exchanger tube
- liquid metal
- steam generator
- 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
Links
- 229910001338 liquidmetal Inorganic materials 0.000 title claims description 7
- 238000010438 heat treatment Methods 0.000 title description 3
- 239000007788 liquid Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 description 34
- 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 24
- 229910052708 sodium Inorganic materials 0.000 description 24
- 239000011734 sodium Substances 0.000 description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 230000000694 effects Effects 0.000 description 7
- 239000007795 chemical reaction product Substances 0.000 description 6
- 238000007664 blowing Methods 0.000 description 5
- NASFKTWZWDYFER-UHFFFAOYSA-N sodium;hydrate Chemical compound O.[Na] NASFKTWZWDYFER-UHFFFAOYSA-N 0.000 description 5
- 230000002265 prevention Effects 0.000 description 4
- 241000270666 Testudines Species 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- 210000001061 forehead Anatomy 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/06—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being molten; Use of molten metal, e.g. zinc, as heat transfer medium
- F22B1/063—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being molten; Use of molten metal, e.g. zinc, as heat transfer medium for metal cooled nuclear reactors
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- High Energy & Nuclear Physics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】
本発明は、伝熱管下降部を有するナトリウム加熱蒸気発
生器にかかり、とくに伝熱管下降部の熱遮蔽構造に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sodium heated steam generator having a descending section of a heat exchanger tube, and particularly relates to a heat shielding structure for the descending section of the heat exchanger tube.
第1図は従来の高速増殖炉用ナトリウム加熱蒸気発生器
の縦断面図を示す。FIG. 1 shows a longitudinal cross-sectional view of a conventional sodium-heated steam generator for a fast breeder reactor.
図において、1は胴体、2は内部胴体、3はへりカルコ
ィル伝熱管、4は熱遮蔽層、5は熱遮蔽板、6は対流防
止板、7は伝熱管下降部、8はガス吹込み管、9はナト
リウムオーバフローノズル、10は放出系ノズル、11
は伝熱管上昇部、12はナトリウム液面、13は給水入
口管板、I4は給水入口ノズル、15は蒸気出口管板、
16は蒸気出口ノズル、17はナトリウム入口ノズル、
18は上部平管板、19はカバーガスノズル、20はナ
トリウム出口ノズル、21はカバーガス領域、22はナ
トリウム分配管である。In the figure, 1 is the body, 2 is the internal body, 3 is the hemical coil heat exchanger tube, 4 is the heat shield layer, 5 is the heat shield plate, 6 is the convection prevention plate, 7 is the descending part of the heat exchanger tube, 8 is the gas blowing pipe , 9 is a sodium overflow nozzle, 10 is a discharge system nozzle, 11
12 is the rising part of the heat transfer tube, 12 is the sodium liquid level, 13 is the water supply inlet tube plate, I4 is the water supply inlet nozzle, 15 is the steam outlet tube plate,
16 is a steam outlet nozzle, 17 is a sodium inlet nozzle,
18 is an upper flat tube plate, 19 is a cover gas nozzle, 20 is a sodium outlet nozzle, 21 is a cover gas area, and 22 is a sodium distribution pipe.
加熱媒体である高温液体金属ナトリウムは、ナトリウム
入口ノズル17より入り、内部胴体2と熱遮蔽板5の間
に設けられた半リング状のナトリウム分配管22により
分配され、ヘリカルコィル伝熱管3により構成される管
東部を流下し、伝熱管内の水−蒸気と熱交換し、低温と
なって胴体下部鏡板に取付けられたナトリウム出口ノズ
ル20より流出する。一方給水は胴体上部に取付けられ
た給水入口ノズル14より流入し、管板13で各伝熱管
に分配され、胴体1と熱遮蔽板5との間の環状領域を一
旦流下し、胴体下部でUターンし、熱遮蔽板5と内部胴
体2の環状領域において軸方向および半径方向とも規則
的なピッチでへりカルコィル状に巻かれた伝熱管3内を
上昇する。High-temperature liquid metal sodium, which is a heating medium, enters through the sodium inlet nozzle 17 and is distributed by a half-ring-shaped sodium distribution pipe 22 provided between the internal body 2 and the heat shield plate 5, and is composed of a helical coil heat transfer tube 3. The sodium flows down the eastern part of the tube, exchanges heat with the water-steam in the heat transfer tube, becomes low temperature, and flows out from the sodium outlet nozzle 20 attached to the lower fuselage end plate. On the other hand, the water supply flows in from the water supply inlet nozzle 14 attached to the upper part of the fuselage, is distributed to each heat exchanger tube by the tube plate 13, flows once through the annular area between the fuselage 1 and the heat shield plate 5, and then flows into the lower part of the fuselage. The heat exchanger tube 3 turns and rises inside the heat exchanger tube 3 which is wound in a helical coil shape at regular pitches in both the axial and radial directions in the annular region of the heat shield plate 5 and the inner body 2.
この時低温で流入した給水は管外を流下する高温のナト
リウムと熱交換し、予熱沸騰、過熱され、高圧、高温の
過熱蒸気となって蒸気出口管板15に集められ、蒸気出
口ノズル16よりタービン(図示せず)へ送られる。本
蒸気発生器は加熱媒体に金属ナトリウムが使用されるこ
とから、伝熱管または伝熱管一瞥板接合部などの破損に
より水が管外に漏洩することは許されず、安全上給水入
口管板13および蒸気出口管板15をカバーガス領域2
11こ設け、急激な過渡変化によるナトリウム液繭亀2
の変動に対しても過度の熱衝撃が加わることのないよう
に配慮されている。At this time, the feed water flowing in at a low temperature exchanges heat with the high-temperature sodium flowing down outside the tube, is preheated to boiling, is superheated, becomes high-pressure, high-temperature superheated steam, is collected in the steam outlet tube plate 15, and is then passed through the steam outlet nozzle 16. to a turbine (not shown). Since this steam generator uses metallic sodium as the heating medium, it is not allowed for water to leak out of the tubes due to damage to the heat exchanger tubes or the heat exchanger tube plate joints, etc., and for safety reasons, water inlet tube plate 13 and Steam outlet tube plate 15 covers gas area 2
Sodium liquid cocoon turtle 2 created by rapid transient changes.
Care has been taken to ensure that excessive thermal shock is not applied even in response to fluctuations in temperature.
また給水入口ノズル14および蒸気出口ノズル16が上
部平板18に取付けられ、管東部が上部平板18から支
持され、保守、点検の時に胴体1から容易に引抜ける構
造となっている。さらに、万一「伝熱管が破断した場合
には、漏洩した水と管外のナトリウムが爆発的に反応し
、その際発生した高熱と水素ガス等の反応生成物により
蒸気発生器内の圧力が上昇するが、これによる胴体の破
裂を防止するため、所定の圧力まで上昇すれば放出系ノ
ズル亀0の出口に設けられたラプチャデスク(図示せず
)が破裂し、放出系ノズル10を通って反応生成物を放
出させる構造となつている。Further, the water supply inlet nozzle 14 and the steam outlet nozzle 16 are attached to the upper flat plate 18, and the eastern part of the pipe is supported from the upper flat plate 18, so that it can be easily pulled out from the body 1 during maintenance and inspection. Furthermore, in the event that the heat transfer tube ruptures, the leaked water and the sodium outside the tube will react explosively, and the pressure inside the steam generator will increase due to the high heat and reaction products such as hydrogen gas. However, in order to prevent the fuselage from bursting due to this, when the pressure rises to a predetermined level, a rupture disk (not shown) provided at the outlet of the discharge system nozzle turtle 0 ruptures, and the rupture disk passes through the discharge system nozzle 10. It has a structure that releases reaction products.
このような蒸気発生器においては、給水ノズル14およ
び蒸気出口ノズル16は蒸気発生器上部に設けられてい
るため、必然的に伝熱管下降部7を有することになる。In such a steam generator, since the water supply nozzle 14 and the steam outlet nozzle 16 are provided in the upper part of the steam generator, the heat exchanger tube descending section 7 is inevitably provided.
ところで「本伝熱管下降部7では給水の吸熱量を低く保
つ必要がある。その理由は伝熱管下降部7の給水の吸熱
量が増大し、管内で給水の沸騰が起こると、蒸気発生器
の運転上きわめて有害な伝熱管内水−蒸気の流動不安定
現象の発生を招く恐れがあるからである。そのため、従
来から伝熱管下降部7とへIJカルコィル伝熱管部3と
の間に二重円筒状の熱遮蔽板5を設け、その間の環状領
域にガスを封入して熱遮蔽層4となし、ヘリカルコィル
伝熱警部3からの入熱量を小さくしている。By the way, it is necessary to keep the amount of heat absorbed by the feed water low in the descending section 7 of the heat exchanger tube.The reason for this is that when the amount of heat absorbed by the supply water in the descending section 7 of the heat exchanger tube increases and boiling of the feed water occurs in the tube, the steam generator This is because there is a risk of causing unstable water-steam flow within the heat exchanger tube, which is extremely harmful to operation.For this reason, conventionally, a double-walled A cylindrical heat shield plate 5 is provided, and a gas is sealed in an annular region therebetween to form a heat shield layer 4, thereby reducing the amount of heat input from the helical coil heat transfer section 3.
第2図は第1図における0ーロ矢視図である。FIG. 2 is a view taken along the 0--ro arrow in FIG. 1.
第3図は従来の伝熱管下降部における熱遮蔽構造の詳細
を示す。二重円筒状の熱遮蔽板5の間の環状領域へ、ガ
ス吹込み管8を通してガスを送り、ナトリウム液面23
をガス逃し穴28の上端まで押し下げ、余分なガスはガ
ス逃し穴28より抜け出る構造となっている。このよう
な伝熱管下降部の熱遮蔽構造においては「熱遮蔽板5の
下端から高温のナトリウムが流入し〜自然対流により伝
熱管軸方向に流動し、熱遮蔽効果を大幅に損うため〜対
流防止板6を適度な間隔で設けている。FIG. 3 shows details of the heat shielding structure in the descending section of the conventional heat exchanger tube. Gas is sent through the gas blowing pipe 8 to the annular area between the double cylindrical heat shield plates 5, and the sodium liquid level 23 is
is pushed down to the upper end of the gas relief hole 28, and excess gas escapes from the gas relief hole 28. In such a heat shielding structure for the descending part of the heat exchanger tube, "high temperature sodium flows from the lower end of the heat shield plate 5 ~ flows in the axial direction of the heat exchanger tube due to natural convection, significantly impairing the heat shielding effect ~ convection" Prevention plates 6 are provided at appropriate intervals.
このような対流防止板6を多数、しかもナトリウム流路
を完全に塞ぐように設ければ大きな熱遮蔽効果を得るこ
とができる。しかし、一方し伝熱管下降部7におけるナ
トリウム−水反応事故に対する対策も考慮しなければな
らない。すなわち〜伝熱管下降部7においてナトリウム
−水反応事故が生じた場合、反応生成物がすみやかに、
放出系ノズル10へ流出できるよう伝熱管下降部7まわ
りのナトリウム流路の流動抵抗を極力小さくする必要が
ある。したがって、従来の熱遮蔽構造では対流防止板を
多数設けたり、ナトリウム流路を塞ぐように設けたりす
ることはできず、そのため、十分な熱遮蔽効果を得るこ
とができないという欠点があった。本発明の目的は上記
の欠点を補い、伝熱管下降部における給水の吸熱量が小
さく「 したがって、管内水−蒸気の流動不安定現象が
生じにくく、かつ、ナトリウム−水反応事故に際し、反
応生成物が容易に放出系に流出する伝熱管下降部の熱遮
蔽構造を提供するにある。A large heat shielding effect can be obtained by providing a large number of such convection prevention plates 6 so as to completely block the sodium flow path. However, on the other hand, measures against a sodium-water reaction accident in the descending section 7 of the heat exchanger tube must also be taken into consideration. In other words, if a sodium-water reaction accident occurs in the descending section 7 of the heat exchanger tube, the reaction product will quickly
It is necessary to minimize the flow resistance of the sodium flow path around the descending section 7 of the heat exchanger tube so that the sodium can flow out to the discharge system nozzle 10. Therefore, in the conventional heat shielding structure, it is not possible to provide a large number of convection prevention plates or to block the sodium flow path, and therefore, there is a drawback that a sufficient heat shielding effect cannot be obtained. The purpose of the present invention is to compensate for the above-mentioned drawbacks, and to provide a heat exchanger that has a small amount of heat absorbed by the feed water in the descending section of the heat exchanger tube. The object of the present invention is to provide a heat shielding structure for a descending portion of a heat exchanger tube from which heat can easily flow out into a discharge system.
本発明の特徴は、従来の円筒状の熱遮蔽板に換え、伝熱
管下降部鯛方向に沿って、下部にガスを溜めることがで
きる形状の傾斜板を多数設け熱遮蔽効果を得るとともに
も万一、ナトリウム−水反応事故が伝熱管下降部で発生
しても「各傾斜板の間隙よりへりカルコイル伝熱都側へ
反応生成物を排除し「放出系へ容易に流出させる構造と
したことにある。The feature of the present invention is that instead of the conventional cylindrical heat shielding plate, a large number of inclined plates are provided along the direction of the descending portion of the heat exchanger tube, each having a shape that allows gas to be stored at the bottom to obtain a heat shielding effect. 1. Even if a sodium-water reaction accident occurs in the descending section of the heat transfer tube, the structure is designed to expel the reaction products from the gap between each inclined plate toward the edge of the calcoil heat transfer tube, allowing them to easily flow out to the release system. be.
第4図は本発明になる伝熱管下降部熱遮蔽構造の実施例
を示す斜視図である。FIG. 4 is a perspective view showing an embodiment of the heat shielding structure for the descending portion of the heat exchanger tube according to the present invention.
第5図は第4図の縦断面を示す。第4図および第5図に
おいて〜 1は胴体ト4は熱遮蔽層、7は伝熱管下降部
、8はガス吹込み管、23は熱遮蔽層ナトリウム液面、
24はガス溜め懐斜板、26は外部胴体である。伝熱管
下降部7まわりの空間は管軸方向に沿って多数のガス溜
め傾斜板24と外部且同26で仕切られている。煩斜板
の関口30は下段のものから順次その蓬が小さいものに
しておく。ガス吹込み管8よりガスを送り、まず,最下
段のガス溜め傾斜板下部にガスを溜めると余ったガスは
気泡となって上昇する。ガス溜の煩斜板24は上段にな
るにつれて水平方向により長くつき出しているので、下
段から上昇したガスの気泡は上段の傾斜坂下部に溜めら
れる。こうして、ガスを送り続けることにより、すべて
のガス溜め傾斜板24の下部にガス層を形成させること
ができる。また、伝熱管下降部7とガス溜め傾斜板24
とはガス溜め傾斜板支持臭25を介して接合し、下段の
ガスが上段へ漏洩しないようにする。ガス溜め傾斜板2
4のピッチ、傾斜角、先端の長さ等の寸法を適当に決定
すれ‘ま、伝熱管下降部7の周囲をほぼ完全にガス層に
することができ、より熱遮蔽効果が得られる。FIG. 5 shows a longitudinal section of FIG. 4. In FIGS. 4 and 5, ~ 1 is the body torso 4 is the heat shield layer, 7 is the descending part of the heat transfer tube, 8 is the gas blowing pipe, 23 is the sodium liquid level of the heat shield layer,
24 is a gas reservoir swash plate, and 26 is an external fuselage. The space around the descending portion 7 of the heat exchanger tube is partitioned along the tube axis direction by a large number of gas reservoir inclined plates 24 and an external gas reservoir inclined plate 26 . Sekiguchi 30 of the sloping board are arranged in order from the bottom one to the smallest one. Gas is sent through the gas blowing pipe 8, and when the gas is first stored in the lower part of the lowest gas reservoir inclined plate, the remaining gas becomes bubbles and rises. Since the oblique plate 24 of the gas reservoir protrudes longer in the horizontal direction toward the upper stage, gas bubbles rising from the lower stage are collected at the lower part of the slope of the upper stage. In this way, by continuing to feed the gas, a gas layer can be formed at the bottom of all the gas reservoir inclined plates 24. In addition, the descending part 7 of the heat exchanger tube and the gas reservoir inclined plate 24
and are connected via the gas reservoir inclined plate support 25 to prevent gas from the lower stage from leaking to the upper stage. Gas reservoir inclined plate 2
By appropriately determining the pitch, angle of inclination, length of the tip, etc. of heat exchanger tube 4, the periphery of descending portion 7 of the heat exchanger tube can be almost completely covered with a gas layer, and a better heat shielding effect can be obtained.
ガス溜め傾斜板24と外部胴体26が囲む小室は一方が
へりカルコィル伝熱管部に開□している。One side of the small chamber surrounded by the gas reservoir inclined plate 24 and the external body 26 is open to the calcoil heat exchanger tube section.
万一、伝熟管下降部7で水が漏洩し、ナトリウム−水反
応が発生した場合、反応生成物は上記閉口部を経て、ヘ
リカルコィル伝熱管側のナトリウム流路へ流出するため
ト流動抵抗が少なく、容易こ放出系へ排出することがで
きる。本発明はこのように構成され作用をするので次の
効果を奏することができる。In the unlikely event that water leaks in the descending section 7 of the tube and a sodium-water reaction occurs, the reaction product will flow through the closed section and flow into the sodium flow path on the helical coil heat transfer tube side, increasing the flow resistance. It can be easily discharged into the release system. Since the present invention is configured and operates in this manner, it can achieve the following effects.
{1’伝熱管下降部のまわりをほぼ完全にガス層とする
ことができるので、ヘリカルコイル伝熱管側からの入熱
に対し、熱遮蔽効果が大きい。{1' Since the lower part of the heat exchanger tube can be almost completely surrounded by a gas layer, the heat shielding effect is great against heat input from the helical coil heat exchanger tube side.
【21 伝熱管下降部における水漏洩で発生したナトリ
ウム−水反応に対して、反応生成物をへりカルコィル伝
熱管側のナトリウム流路に流出させることができるため
、流動抵抗が少なく、放出系への排出がすみやかに行な
われる。[21] In response to the sodium-water reaction that occurs due to water leakage in the descending section of the heat transfer tube, the reaction product can flow out into the sodium flow path on the side of the calcoil heat transfer tube, so there is little flow resistance and there is no flow to the release system. Evacuation occurs quickly.
第1図は従釆の高速増殖炉用ナトリウム加熱蒸気発生器
の縦断面、第2図は第1図の0−ロ矢視図、第3図は従
来の伝熱管下降部熱遮蔽構造を示す縦断面図、第4図は
本発明になる実施例を示す斜視図、第5図は第4図の縦
断面図である。
4・・・・・・熱遮蔽層、7…・・・伝熱管下降部、8
・・…・ガス吹き込み管、24・・・・・・ガス溜め煩
斜板、26…・・・外部胴体、30a,30b……額斜
板の開口。
第2図
第3図
第1図
第4図
第5図Figure 1 shows a vertical cross-section of a sodium-heated steam generator for a secondary fast breeder reactor, Figure 2 shows a view from the 0-B arrow in Figure 1, and Figure 3 shows a conventional heat shielding structure for the descending part of heat transfer tubes. 4 is a perspective view showing an embodiment of the present invention, and FIG. 5 is a longitudinal sectional view of FIG. 4. 4...Heat shielding layer, 7...Heat transfer tube descending part, 8
...... Gas blowing pipe, 24... Gas reservoir swash plate, 26... External body, 30a, 30b... Opening of forehead swash plate. Figure 2 Figure 3 Figure 1 Figure 4 Figure 5
Claims (1)
いて、液体金属液深方向に前記伝熱管下降部を横断し、
かつ下方に傾斜する台形錐状の傾斜板を複数段設け、上
段の傾斜板の開口径は下段の傾斜板の開口径より小とし
、これら傾斜板相互間にガスを溜めた熱遮蔽層を設ける
ことを特徴とする液体金属加熱蒸気発生器伝熱管下降部
の熱遮蔽装置。 2 熱遮蔽層の開口は液体金属面で閉ざされていること
を特徴とする特許請求の範囲第1項記載の液体金属加熱
蒸気発生器伝熱管下降部の熱遮蔽装置。[Scope of Claims] 1. In a liquid metal heated steam generator having a descending section of a heat transfer tube, the descending section of the heat transfer tube is crossed in a depth direction of the liquid metal liquid,
In addition, a plurality of trapezoidal pyramid-shaped sloped plates that slope downward are provided, the opening diameter of the upper sloped plate is smaller than the opening diameter of the lower sloped plate, and a heat shielding layer containing gas is provided between these sloped plates. A heat shielding device for a descending section of a heat transfer tube of a liquid metal heated steam generator, characterized in that: 2. A heat shielding device for a descending portion of a heat exchanger tube of a liquid metal heated steam generator according to claim 1, wherein the opening of the heat shielding layer is closed by a liquid metal surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13468077A JPS606443B2 (en) | 1977-11-11 | 1977-11-11 | Heat shielding device for descending section of heat exchanger tube of liquid metal heating steam generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13468077A JPS606443B2 (en) | 1977-11-11 | 1977-11-11 | Heat shielding device for descending section of heat exchanger tube of liquid metal heating steam generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5467801A JPS5467801A (en) | 1979-05-31 |
| JPS606443B2 true JPS606443B2 (en) | 1985-02-18 |
Family
ID=15134051
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13468077A Expired JPS606443B2 (en) | 1977-11-11 | 1977-11-11 | Heat shielding device for descending section of heat exchanger tube of liquid metal heating steam generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS606443B2 (en) |
-
1977
- 1977-11-11 JP JP13468077A patent/JPS606443B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5467801A (en) | 1979-05-31 |
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