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JPS5848880B2 - pressure tube reactor - Google Patents
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JPS5848880B2 - pressure tube reactor - Google Patents

pressure tube reactor

Info

Publication number
JPS5848880B2
JPS5848880B2 JP54134199A JP13419979A JPS5848880B2 JP S5848880 B2 JPS5848880 B2 JP S5848880B2 JP 54134199 A JP54134199 A JP 54134199A JP 13419979 A JP13419979 A JP 13419979A JP S5848880 B2 JPS5848880 B2 JP S5848880B2
Authority
JP
Japan
Prior art keywords
water
heavy water
moderator
temperature
pressure tube
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
Application number
JP54134199A
Other languages
Japanese (ja)
Other versions
JPS5658698A (en
Inventor
久秀 名取
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP54134199A priority Critical patent/JPS5848880B2/en
Publication of JPS5658698A publication Critical patent/JPS5658698A/en
Publication of JPS5848880B2 publication Critical patent/JPS5848880B2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 本発明は圧力管型原子炉の給水加熱に関する。[Detailed description of the invention] The present invention relates to feed water heating for pressure tube nuclear reactors.

従来、原子炉の給水加熱はタービンから抽気した蒸気に
より復水器からの水(給水)を加熱している。
Conventionally, feed water in a nuclear reactor is heated by heating water (feed water) from a condenser using steam extracted from a turbine.

第1図&’!550MWt級の圧力管型原子炉の主蒸気
系および給水系を示すもので、高圧タービン1、低圧タ
ービン2,3、発電機4、湿分分離器5、復水器6、空
気抽出器7、グランド蒸気復水器8、低圧給水加熱器9
,10,11、高圧給水加熱器12,13、復水ポンプ
14、給水ポンプ15とを備えている。
Figure 1&'! This shows the main steam system and water supply system of a 550 MWt class pressure tube reactor, including a high pressure turbine 1, low pressure turbines 2 and 3, a generator 4, a moisture separator 5, a condenser 6, an air extractor 7, Gland steam condenser 8, low pressure feed water heater 9
, 10, 11, high-pressure feed water heaters 12, 13, a condensate pump 14, and a water feed pump 15.

そして蒸気ドラムから出た高圧蒸気16は高圧タービン
1に入り、この高圧タービン1から出た一部低圧蒸気1
7は湿分分離器5により湿分を取り除かれたうえで低圧
タービン2,3に入る。
The high-pressure steam 16 coming out of the steam drum then enters the high-pressure turbine 1, and a portion of the low-pressure steam 1 that comes out of this high-pressure turbine 1
7 enters the low pressure turbines 2 and 3 after moisture is removed by the moisture separator 5.

前記低圧タービン2,3から出た蒸気18と高圧タービ
ン1から出た一部蒸気19は復水器6に送られる。
Steam 18 discharged from the low pressure turbines 2 and 3 and a portion of steam 19 discharged from the high pressure turbine 1 are sent to a condenser 6.

また給水25を加熱するために、高圧タービン1および
低圧タービン2,3から蒸気20,21 ,22,23
,24が抽気され、対応する低圧給水加熱器9,10,
11および高圧給水加熱器12.13に送られ、前記蒸
気20〜24は給水を加熱後、水26となり、復水器6
に入る。
Also, in order to heat the feed water 25, steam 20, 21, 22, 23 is generated from the high pressure turbine 1 and the low pressure turbines 2, 3.
, 24 are bled and the corresponding low pressure feed water heaters 9, 10,
11 and high-pressure feed water heaters 12 and 13, the steam 20 to 24 heats the feed water, becomes water 26, and is sent to the condenser 6.
to go into.

前記5 5 0 MWt級の圧力管型原子炉の定格出力
時においては、約9 1 0 t/hの給水が第1段の
低圧給水加熱器9で約35℃から約59℃まで加熱され
、第2段以後の給水加熱器10〜13で約182℃まで
加熱される。
At the rated output of the 550 MWt class pressure tube nuclear reactor, about 910 t/h of feed water is heated from about 35°C to about 59°C in the first stage low pressure feed water heater 9, The feed water heaters 10 to 13 in the second and subsequent stages heat the water to about 182°C.

一方、圧力管型原子炉においては、核分裂によって発生
した熱エネルギーのうち約6%は圧力管の外側の減速材
(重水)中で発生する。
On the other hand, in a pressure tube reactor, about 6% of the thermal energy generated by nuclear fission is generated in the moderator (heavy water) outside the pressure tube.

すなわち5 5 0 MWt級の原子炉では定格出力時
に約33MWの熱が重水中で発生する。
That is, in a 550 MWt class nuclear reactor, approximately 33 MW of heat is generated in heavy water at the rated output.

この熱は流量1 4 0 0 t/hの重水の温度を約
20℃上昇させ、重水の炉心出口温度を約70℃とする
This heat raises the temperature of heavy water at a flow rate of 1400 t/h by about 20°C, making the core exit temperature of the heavy water about 70°C.

第2図に550MWt級圧力管型原子炉の重水循環、系
統を示す。
Figure 2 shows the heavy water circulation and system of a 550MWt class pressure tube reactor.

この第2図に示される重水循環系統は炉心27、重心ダ
ンプ・タンク28、重水循環ポンプ29、重水冷却器3
0を有し、炉心27で約70℃まで温度上昇した重水3
1は2基の重水冷却器30(1基あたりの伝熱面積は約
100077L″)により約49℃になるまで冷却され
る。
The heavy water circulation system shown in FIG. 2 includes a reactor core 27, a center of gravity dump tank 28, a heavy water circulation pump 29, and a heavy water cooler 3.
0, and the temperature of heavy water 3 rose to approximately 70°C in the core 27.
1 is cooled to about 49° C. by two heavy water coolers 30 (heat transfer area per one is about 100077 L″).

重水冷却器30から出た低温の重水32の一部33はポ
イズン供給・除去系へ送られ、他の一部は炉心2Tに戻
される。
A portion 33 of the low-temperature heavy water 32 discharged from the heavy water cooler 30 is sent to the poison supply/removal system, and the other portion is returned to the reactor core 2T.

重水ダンプ28には前記ポイズン供給・除去系から重水
34が戻される。
Heavy water 34 is returned to the heavy water dump 28 from the poison supply/removal system.

重水冷却器30に入る高温の重水31の熱は補機冷却水
35を介して海水にすてられる。
The heat of the high-temperature heavy water 31 entering the heavy water cooler 30 is dissipated into seawater via the auxiliary equipment cooling water 35.

本発明の目的は重水中で発生した熱を給水加熱に用い、
タービンからの蒸気抽出量を減らすことにより発電効率
の高い圧力管型原子炉を提供することにある。
The purpose of the present invention is to use the heat generated in heavy water to heat feed water,
The object of the present invention is to provide a pressure tube nuclear reactor with high power generation efficiency by reducing the amount of steam extracted from the turbine.

本発明の特徴は冷却材と減速材が分離されている圧力管
型原子炉において、低圧給水加熱器列の前段に熱交換器
が設けられ、該熱交換器の1次側には減速材もしくは減
速材で加熱された流体が、2次側には給水がそれぞれ通
過せしめられ、炉心で加熱された前記減速材もしくは減
速材で加熱された流体の熱により給水が加熱され、かつ
タービンから抽気される蒸気が減少せしめられていると
ころに存し、この構成によりタービンからの蒸気抽出量
を減少せしめることによって発電効率の高い圧力管型原
子炉を得たものである。
The feature of the present invention is that in a pressure tube nuclear reactor in which the coolant and the moderator are separated, a heat exchanger is provided at the front stage of the low-pressure feed water heater row, and the moderator or the moderator is provided on the primary side of the heat exchanger. The fluid heated by the moderator is passed through the secondary side, and the feed water is passed through the secondary side, and the feed water is heated by the heat of the moderator heated in the core or the fluid heated by the moderator, and air is extracted from the turbine. This configuration reduces the amount of steam extracted from the turbine, resulting in a pressure tube nuclear reactor with high power generation efficiency.

以下本発明を図面に基づいて説明する。The present invention will be explained below based on the drawings.

第3図は本発明の一実施例を示すもので、熱交換器36
、重水冷却器37が設置されている外は前記第1図に示
される圧力型原子炉と同様である。
FIG. 3 shows an embodiment of the present invention, in which a heat exchanger 36
This reactor is similar to the pressure reactor shown in FIG. 1, except that a heavy water cooler 37 is installed.

前記熱交換器36は低圧給水加熱器列の前段、すなわち
第1図に示される第1段の給水加熱器9の取り付け位置
に設けられ、熱交換器36の1次側には第2図に示され
る炉心27で温度上昇された高温の重水31が通過せし
められ、2次側にはグランド蒸気復水器8から低圧給水
加熱器10,11・・・を含む低圧給水加熱器列に向う
給水25が通過せしめられる。
The heat exchanger 36 is installed at the front stage of the row of low-pressure feed water heaters, that is, at the installation position of the first stage feed water heater 9 shown in FIG. High-temperature heavy water 31 whose temperature has been raised in the shown reactor core 27 is passed through, and on the secondary side, water is supplied from the grand steam condenser 8 to a row of low-pressure feedwater heaters including low-pressure feedwater heaters 10, 11, . . . 25 is allowed to pass.

前記冷却器37は重水31の流れ方向において前記熱交
換器36の下流側に設けられており、重水冷却器37の
1次側には熱交換器36から出た重水が通過せしめられ
、2次側には補機冷却水35が送られる。
The cooler 37 is provided on the downstream side of the heat exchanger 36 in the flow direction of the heavy water 31, and the heavy water discharged from the heat exchanger 36 is passed through the primary side of the heavy water cooler 37, and the secondary Auxiliary cooling water 35 is sent to the side.

また重水冷却器37は重水冷却器出口温度を検出し、補
機冷却水35の流量を調整して重水冷却器出口炉心入口
の重水32の温度を設定温度に保つものである。
The heavy water cooler 37 detects the heavy water cooler outlet temperature and adjusts the flow rate of the auxiliary equipment cooling water 35 to maintain the temperature of the heavy water 32 at the heavy water cooler outlet and core inlet at a set temperature.

重水冷却器37の熱交換量は当然熱交換器36より小さ
くなる。
Naturally, the heat exchange amount of the heavy water cooler 37 is smaller than that of the heat exchanger 36.

前述構成の本発明圧力管型原子炉では従来、給水25を
加熱するために低圧タービンから抽気していた第1段の
低圧給水加熱用の蒸気20は抽気する必要はなくなり、
タービンの回転に使用できるので発電効率を向上させる
ことができる。
In the pressure tube nuclear reactor of the present invention having the above-mentioned configuration, the steam 20 for heating the low-pressure feedwater in the first stage, which was conventionally extracted from the low-pressure turbine to heat the feedwater 25, no longer needs to be extracted.
Since it can be used to rotate a turbine, power generation efficiency can be improved.

1例として550MWt級の圧力管型原子炉を考える。As an example, consider a 550 MWt class pressure tube reactor.

熱交換器36には伝熱面積1500m”,熱通過率1
0 3Kcal/ m h’Cの向流型を用いると、定
格出力時には流量9 1 0 t/hの給水25の温度
を約35℃から約58.5℃まで上昇させることができ
、流量t400t/hの重水31の温度(熱交換器出口
温度)を69℃から約53.8°Cまで下げることが可
能となる。
The heat exchanger 36 has a heat transfer area of 1500 m'' and a heat transfer rate of 1.
By using a counterflow type with a flow rate of 0.3 Kcal/m h'C, the temperature of the water supply 25 with a flow rate of 910 t/h can be raised from approximately 35°C to approximately 58.5°C at the rated output, and the flow rate is 400 t/h. It becomes possible to lower the temperature of the heavy water 31 (heat exchanger outlet temperature) from 69°C to about 53.8°C.

また25%出力時には2 5 6 t/hの給水25の
温度を40℃から約54.9℃まで上昇させ、1400
t/hの重水31の温度を55℃から約52.3℃まで
下げることができる。
In addition, at 25% output, the temperature of the 256 t/h water supply 25 was increased from 40°C to approximately 54.9°C, and the temperature was increased to 1400°C.
The temperature of heavy water 31 per t/h can be lowered from 55°C to about 52.3°C.

タービンから抽気した蒸気のみで加熱する従来の圧力管
型原子炉では、第1段の低圧給水加熱器の出口温度は定
格出力時は約59℃、25%出力時は41’Cであるの
で、本発明圧力管型原子炉は定格出力時には従来のもの
とほぼ同等な温度が得られる。
In a conventional pressure tube nuclear reactor that heats only with steam extracted from the turbine, the outlet temperature of the first stage low-pressure feedwater heater is approximately 59°C at rated output and 41'C at 25% output. The pressure tube type nuclear reactor of the present invention can obtain temperatures almost equivalent to those of conventional reactors at rated output.

また低出力時には従来のものより高い給水温度となるが
、定格出力時の第1段の給水加熱器出口温度58.5℃
よりは低いので給水ポンプのキャビテーションなどの問
題はおこらない。
Also, at low output, the feed water temperature is higher than the conventional one, but at rated output the first stage feed water heater outlet temperature is 58.5℃.
Because it is lower than the above, problems such as cavitation of the water supply pump do not occur.

また炉心側としても25%出力時に給水温度が20℃上
昇したとしても、炉心人口エンタルピは2 8 3.
5 Kcal/ kgから2 8 4. 8 Kcan
/kgになる程度で出力分布、熱的制限値への影警は
小さく問題ない。
Also, on the core side, even if the feed water temperature increases by 20°C at 25% power, the core population enthalpy will be 2 8 3.
5 Kcal/kg to 2 8 4. 8 Kcan
/kg, the influence on the output distribution and thermal limit value is small and there is no problem.

以上の結果から給水温度に関しては従来のものと同等な
効果が得られる。
From the above results, the same effect as the conventional system can be obtained regarding the water supply temperature.

つぎに重水温度について考える。Next, let's consider the temperature of heavy water.

熱交換器36の出口の重水温度は炉出力によって異なり
定格出力時、25%出力時で従来の圧力管型原子炉の重
水冷却器の出口温度(補機冷却水流量により設定温度4
9℃に制御される)よりそれぞれ約5℃、約3℃高くな
る。
The heavy water temperature at the outlet of the heat exchanger 36 varies depending on the reactor output, and at rated output and 25% output, the outlet temperature of the heavy water cooler of a conventional pressure tube reactor (the set temperature 4 depending on the flow rate of auxiliary cooling water)
The temperatures are approximately 5°C and 3°C higher than the 9°C control temperature, respectively.

したがって重水冷却器37により重水冷却器出口炉心入
口の温度を設定温度になるように補機冷却水35の流量
を変えて調整する。
Therefore, the heavy water cooler 37 adjusts the temperature at the outlet of the heavy water cooler and the inlet of the core by changing the flow rate of the auxiliary cooling water 35 so that it reaches the set temperature.

向流型の重水冷却器の伝熱面積を30Om、熱通過率を
1 03Kcal/ mh’cとし、定格出力時に補機
冷却水35を+250t/h流すことにより重水温度を
53.8℃から約49℃にすることができる。
The heat transfer area of the counter-current heavy water cooler is 30 Om, the heat transfer rate is 103 Kcal/mh'c, and by flowing auxiliary cooling water 35 at +250 t/h at rated output, the heavy water temperature can be reduced from 53.8°C to approximately It can be brought to 49°C.

また25%出力時には約250t/h流すことにより重
水温度を52.3℃から約49℃にすることができる。
Furthermore, at 25% output, the heavy water temperature can be raised from 52.3°C to about 49°C by flowing about 250 t/h.

つぎにタービンから抽気蒸気量を減らした場合の発電気
出力の増加量について述べる。
Next, we will discuss the amount of increase in power generation output when the amount of steam extracted from the turbine is reduced.

定格出力時に第1図において第l段の低圧給水加熱器9
に抽気する蒸気20のエンクルピは566KCal/k
g、流量は約29t/hである。
At rated output, the low pressure feed water heater 9 of stage I in Fig. 1
The enclosing power of 20 steam to be extracted is 566 KCal/k.
g, the flow rate is approximately 29 t/h.

この蒸気がタービンの回転に用いられて5 3 4.
9 Kcal /kgのエンタルピをもつ蒸気18とな
った場合(タービンから排出する蒸気のエンタルピはタ
ービンからの抽気蒸気量を減らした場合でも変らないと
仮定)、発電気出力は従来の発電機出力1 6 5 M
Weに比べて約0.6%増大する。
This steam is used to rotate the turbine 5 3 4.
When the steam 18 has an enthalpy of 9 Kcal/kg (assuming that the enthalpy of the steam discharged from the turbine does not change even if the amount of extracted steam from the turbine is reduced), the generated electricity output is equal to the conventional generator output 1 6 5 M
It increases by about 0.6% compared to We.

なお第1図,第2図と第3図とで同一部材には同じ符号
を付して説明している。
Note that the same members are designated by the same reference numerals in FIGS. 1, 2, and 3 for explanation.

第4図は本発明の他の実施例を示すものであって、重水
系統と給水系統を別建屋に設置した場合の実施例を示す
FIG. 4 shows another embodiment of the present invention, in which the heavy water system and the water supply system are installed in separate buildings.

圧力管型原子炉においては通常重水系統は原子炉建屋内
に、給水加熱器はタービン建屋に配置される。
In a pressure tube reactor, the heavy water system is usually located in the reactor building, and the feedwater heater is located in the turbine building.

そこで第4図に示す実施例では重水冷却器30と、給水
25を加熱するための熱交換器36との間に、軽水循環
ポンプ39を備える閉ループの軽水循環系統が接続され
ている。
Therefore, in the embodiment shown in FIG. 4, a closed-loop light water circulation system including a light water circulation pump 39 is connected between the heavy water cooler 30 and the heat exchanger 36 for heating the water supply 25.

該軽水循環系統を流れる軽水38は、重水系統の重水冷
却器30で高温の重水31と熱交換され、温度上昇され
た軽水38により給水25を加熱するようにしている。
The light water 38 flowing through the light water circulation system is heat exchanged with high temperature heavy water 31 in the heavy water cooler 30 of the heavy water system, and the water supply 25 is heated by the light water 38 whose temperature has been raised.

これにより重水系統を原子炉建屋内に、給水加熱器をタ
ービン建屋に配置して重水31による給水25の加熱が
可能となる。
This makes it possible to heat the feed water 25 with the heavy water 31 by arranging the heavy water system in the reactor building and the feed water heater in the turbine building.

本発明は以上説明した構戒,作用のもので、高温の重水
を利用して給水を加熱するようにしているので、タービ
ンからの抽気を減少でき、したがって発電効率を向上し
うる効果がある。
The present invention has the above-described structure and function, and uses high-temperature heavy water to heat the water supply, thereby reducing the amount of air extracted from the turbine, thereby improving power generation efficiency.

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

第1図は圧力管型原子炉の主蒸気系および給水系の系統
図、第2図は重水系の系統図である。 第3図は本発明による給水加熱の系統図、第4図は重水
系統と給水系統とを別建屋に配置した本発明による給水
加熱の系統図である。 io,1i・・・・・・低圧給水加熱器、21,22・
・・・・・低圧タービンから抽気した蒸気、25・・・
・・・給水、26・・・・・・給水加熱後の水、27・
・・・・・炉心、30,37・・・・・・重水冷却器か
ら出る重水、35・・・・・・補機冷却水、36・・・
・・・熱交換器、38・・・・・・軽水。
Figure 1 is a system diagram of the main steam system and water supply system of a pressure tube reactor, and Figure 2 is a system diagram of the heavy water system. FIG. 3 is a system diagram of feed water heating according to the present invention, and FIG. 4 is a system diagram of feed water heating according to the present invention in which the heavy water system and the water supply system are arranged in separate buildings. io, 1i...Low pressure water heater, 21, 22.
...Steam extracted from the low pressure turbine, 25...
... Water supply, 26 ... Water after heating the water supply, 27.
...Reactor core, 30,37...Heavy water coming out of the heavy water cooler, 35...Auxiliary equipment cooling water, 36...
...Heat exchanger, 38...Light water.

Claims (1)

【特許請求の範囲】 1 冷却材と減速材が分離されている圧力管型原子炉に
おいて、低圧給水加熱器列の前段に熱交換器が設けられ
、該熱交換器の1次側には減速材もしくは減速材で加熱
された流体が、2次側には給水がそれぞれ通過せしめら
れ、炉心で加熱された前記減速材もしくは減速材で加熱
された流体の熱により給水が加熱され、かつタービンか
ら抽気される蒸気が減少せしめられていることを特徴と
する圧力管型原子炉。 2 前記熱交換器には重水冷却器に連結された閉ループ
の軽水循環系統が接続されており、重水冷却器で加熱さ
れた軽水の熱により給水が加熱されるように構成されて
いることを特徴とする特許請求の範囲第1項記載の圧力
管型原子炉。
[Claims] 1. In a pressure tube nuclear reactor in which the coolant and moderator are separated, a heat exchanger is provided upstream of a row of low-pressure feed water heaters, and a moderator is provided on the primary side of the heat exchanger. The fluid heated by the moderator or the moderator is passed through the secondary side, and the feedwater is heated by the heat of the moderator heated in the core or the fluid heated by the moderator. A pressure tube nuclear reactor characterized by reduced steam extraction. 2. A closed-loop light water circulation system connected to a heavy water cooler is connected to the heat exchanger, and the water supply is heated by the heat of the light water heated by the heavy water cooler. A pressure tube nuclear reactor according to claim 1.
JP54134199A 1979-10-19 1979-10-19 pressure tube reactor Expired JPS5848880B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54134199A JPS5848880B2 (en) 1979-10-19 1979-10-19 pressure tube reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54134199A JPS5848880B2 (en) 1979-10-19 1979-10-19 pressure tube reactor

Publications (2)

Publication Number Publication Date
JPS5658698A JPS5658698A (en) 1981-05-21
JPS5848880B2 true JPS5848880B2 (en) 1983-10-31

Family

ID=15122739

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54134199A Expired JPS5848880B2 (en) 1979-10-19 1979-10-19 pressure tube reactor

Country Status (1)

Country Link
JP (1) JPS5848880B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6689657B2 (en) * 2016-04-18 2020-04-28 日本コークス工業株式会社 Crushing system

Also Published As

Publication number Publication date
JPS5658698A (en) 1981-05-21

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