JP2007160162A - Method for operating power plant - Google Patents
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- JP2007160162A JP2007160162A JP2005357253A JP2005357253A JP2007160162A JP 2007160162 A JP2007160162 A JP 2007160162A JP 2005357253 A JP2005357253 A JP 2005357253A JP 2005357253 A JP2005357253 A JP 2005357253A JP 2007160162 A JP2007160162 A JP 2007160162A
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
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Abstract
Description
本発明は、発電所の運転方法に関し、とくに銅合金を用いた復水系統機器を使用している加圧水型原子力発電所や火力発電所に好適な発電所の運転方法に関する。 The present invention relates to a power plant operation method, and more particularly, to a power plant operation method suitable for a pressurized water nuclear power plant or a thermal power plant using a condensate system apparatus using a copper alloy.
加圧水型原子力発電所や火力発電所において、設置年度が古いプラントでは、プラント構成要素である、復水器、熱交換器等の材料として、伝熱効率の良好な銅合金(アルミニウム黄銅、アルミニウム青銅、キュプロニッケル等)が用いられている。また、蒸気発生器への鉄流入を抑制するため、二次系機器・配管の防食を目的として、ヒドラジンを用いて系統水を脱気し、アンモニア、エタノールアミン(ETA)を用いてpHを9.2程度に制御する全揮発性薬品処理(AVT)が実施されている。 In pressurized water nuclear power plants and thermal power plants, in plants where the installation year is old, copper alloys with good heat transfer efficiency (aluminum brass, aluminum bronze, Cupronickel etc.) are used. In order to suppress iron inflow to the steam generator, the system water is degassed with hydrazine for the purpose of corrosion protection of secondary equipment and piping, and the pH is adjusted to 9 with ammonia and ethanolamine (ETA). All volatile chemical treatment (AVT) controlled to about 2 is implemented.
近年、復水系の系統水浄化の目的で、復水浄化装置、とくに復水ろ過装置の適用が進んでおり、この復水ろ過装置として中空糸膜フィルタの適用が進んでいるが(例えば、特許文献1)、復水器、熱交換器等の系統構成材料に銅合金を適用し且つ全揮発性薬品処理を実施している発電プラントに設置された中空糸膜フィルタは、物理的強度が極端に低下し、中空糸膜フィルタの破断、ひいてはろ過精度の低下が生じている。
上記のような中空糸膜フィルタの物理的強度が急激に低下する要因を種々研究した結果、原因は以下と推定された。
(1)復水系統水中の溶存酸素を低減する目的で添加されるヒドラジンが溶存酸素と反応し過酸化水素を生じる。
(2)生じた過酸化水素は銅合金から溶出する銅イオンと反応し、強力な酸化力を持つ、ヒドロキシルラジカルが発生する。
(3)発生したヒドロキシルラジカルは、中空糸膜フィルタの素材であるポリスルフォンを酸化し、物理的強度を急激に低下させる。
ここで、銅イオンは系統構成材料の銅合金から溶出したものである。
As a result of various studies on the factors that cause a sudden decrease in the physical strength of the hollow fiber membrane filter as described above, the cause was estimated as follows.
(1) Hydrazine added for the purpose of reducing dissolved oxygen in condensate water reacts with dissolved oxygen to produce hydrogen peroxide.
(2) The generated hydrogen peroxide reacts with copper ions eluted from the copper alloy to generate hydroxyl radicals having a strong oxidizing power.
(3) The generated hydroxyl radical oxidizes polysulfone, which is a material of the hollow fiber membrane filter, and sharply lowers the physical strength.
Here, copper ions are eluted from the copper alloy of the system constituent material.
本発明の課題は、上記のような知見に基づき、復水浄化装置に用いられるフィルタ、とくにポリスルフォンからなる中空糸膜フィルタの強度低下を防止し得る発電所の運転方法を提供することにある。 The subject of this invention is providing the operating method of the power plant which can prevent the strength reduction of the filter used for a condensate purification apparatus, especially the hollow fiber membrane filter which consists of polysulfone based on the above knowledge. .
上記課題を解決するために、本発明に係る発電所の運転方法は、復水系統の構成材料に銅合金を使用しかつ全揮発性薬品処理を実施している発電所における運転方法であって、ヒドラジン以外のアルカリ薬品により復水浄化装置入口水のpHを9以上に調整することを特徴とする方法からなる。 In order to solve the above problems, the operation method of the power plant according to the present invention is an operation method in a power plant that uses a copper alloy as a constituent material of the condensate system and performs total volatile chemical treatment. The pH of the condensate purification apparatus inlet water is adjusted to 9 or more with an alkaline chemical other than hydrazine.
すなわち、復水浄化装置、とくに復水ろ過装置の入口水を、ヒドラジン以外のアルカリ薬品でpH9以上に調整することにより、酸化要因となる過酸化水素の分解を促進し、ひいてはヒドロキシルラジカルの発生を抑制し、フィルタ、とくにポリスルフォンからなる中空糸膜フィルタの酸化劣化を低減するものである。 That is, by adjusting the inlet water of the condensate purification apparatus, particularly the condensate filtration apparatus, to pH 9 or higher with an alkaline chemical other than hydrazine, the decomposition of hydrogen peroxide, which is an oxidative factor, is promoted, and thus the generation of hydroxyl radicals is promoted. It suppresses and reduces oxidative degradation of a filter, particularly a hollow fiber membrane filter made of polysulfone.
ここで、ヒドラジン以外のアルカリ薬品でpH9以上に調整するとは、ヒドラジンの添加を排除するものではなく、pHを目標とする9以上に調整するために、ヒドラジン以外のアルカリ薬品を使用するという意味であり、ヒドラジン以外のアルカリ薬品のみでpH9以上に調整する場合と、ヒドラジンを添加した上で更にヒドラジン以外のアルカリ薬品を添加してpH9以上に調整する場合の両方を含む。ヒドラジン以外のアルカリ薬品としては、アンモニアやエタノールアミンを用いることができる。 Here, adjusting to pH 9 or higher with an alkaline chemical other than hydrazine does not exclude the addition of hydrazine, but means that an alkaline chemical other than hydrazine is used to adjust the pH to 9 or higher. There are both cases where the pH is adjusted to 9 or more only with an alkaline chemical other than hydrazine, and cases where the pH is adjusted to 9 or higher by adding an alkaline chemical other than hydrazine after adding hydrazine. As alkaline chemicals other than hydrazine, ammonia or ethanolamine can be used.
また、本発明に係る発電所の運転方法は、復水系統の構成材料に銅合金を使用しかつ全揮発性薬品処理を実施している発電所における運転方法であって、復水浄化装置入口水の溶存酸素を1ppm以下に調整することを特徴とする方法からなる。 The operation method of the power plant according to the present invention is an operation method in a power plant that uses a copper alloy as a constituent material of the condensate system and performs all volatile chemical treatment, and is provided at the inlet of the condensate purification apparatus. It consists of the method characterized by adjusting the dissolved oxygen of water to 1 ppm or less.
すなわち、復水浄化装置、とくに復水ろ過装置の入口溶存酸素を1ppm以下に調整することにより、酸化要因となる過酸化水素の発生を低減し、ひいてはヒドロキシルラジカルの発生を抑制し、フィルタ、とくにポリスルフォンからなる中空糸膜フィルタの酸化劣化を低減するものである。 That is, by adjusting the dissolved oxygen at the inlet of the condensate purification device, particularly the condensate filtration device, to 1 ppm or less, the generation of hydrogen peroxide, which is an oxidative factor, is reduced, and the generation of hydroxyl radicals is suppressed. It is intended to reduce oxidative degradation of a hollow fiber membrane filter made of polysulfone.
溶存酸素を1ppm以下に調整するためには、例えば脱気純水を供給することができる。また、溶存酸素を1ppm以下に調整するために、復水系統および/または給水系統を窒素シールすることもできる。 In order to adjust the dissolved oxygen to 1 ppm or less, for example, degassed pure water can be supplied. Further, in order to adjust the dissolved oxygen to 1 ppm or less, the condensate system and / or the water supply system can be sealed with nitrogen.
また、本発明に係る発電所の運転方法は、復水系統の構成材料に銅合金を使用しかつ全揮発性薬品処理を実施している発電所における運転方法であって、運転前に予め酸化鉄または/および水酸化鉄を復水浄化装置のろ過膜表面に捕捉させ、しかる後に通水処理を行うことを特徴とする方法からなる。 Further, the power plant operating method according to the present invention is a power plant operating method using a copper alloy as a constituent material of the condensate system and carrying out the treatment of all volatile chemicals. It consists of a method characterized in that iron or / and iron hydroxide is trapped on the surface of the filtration membrane of the condensate purification apparatus, and then water passing treatment is performed.
すなわち、復水浄化装置、とくに復水ろ過装置の通水前に予め酸化鉄、水酸化鉄等を中空糸膜フィルタのろ過表面に捕捉させ、生成したヒドロキシルラジカルの酸化に対し、中空糸膜表面を保護し、酸化劣化を抑制するものである。 That is, before passing water through a condensate purification device, in particular before passing through the condensate filtration device, iron oxide, iron hydroxide, etc. are captured in advance on the filtration surface of the hollow fiber membrane filter, and the surface of the hollow fiber membrane against oxidation of the generated hydroxyl radicals. Protects against oxidative degradation.
上記のような本発明に係る発電所の運転方法は、いずれか2つ以上の方法を併用して実施することも可能である。 The operation method of the power plant according to the present invention as described above can be carried out by using any two or more methods in combination.
このような本発明に係る発電所の運転方法は、とくに復水浄化装置にポリスルフォン膜からなるフィルタを用いる場合、中でも、中空糸膜フィルタを用いる場合に有効なものである。 Such a power plant operating method according to the present invention is effective particularly when a filter made of a polysulfone membrane is used in the condensate purification apparatus, and particularly when a hollow fiber membrane filter is used.
本発明に係る発電所の運転方法によれば、中空糸膜フィルタの入口pHを9以上にアンモニア等を用いて調整することにより、ポリスルフォン膜の物理的強度の低下を抑制することができる。また、中空糸膜フィルタの入口溶存酸素を1ppm以下に調整することにより、ポリスルフォン膜の物理的強度の低下を抑制することができる。さらに、中空糸膜フィルタの通水前に予め酸化鉄や水酸化鉄をろ過表面に捕捉させることにより、ポリスルフォン膜の物理的強度の低下を抑制することができる。 According to the operation method of the power plant according to the present invention, it is possible to suppress a decrease in physical strength of the polysulfone membrane by adjusting the inlet pH of the hollow fiber membrane filter to 9 or more using ammonia or the like. Moreover, the fall of the physical strength of a polysulfone membrane can be suppressed by adjusting the inlet dissolved oxygen of a hollow fiber membrane filter to 1 ppm or less. Further, by preliminarily capturing iron oxide or iron hydroxide on the filtration surface before passing through the hollow fiber membrane filter, it is possible to suppress a decrease in physical strength of the polysulfone membrane.
以下に、本発明の望ましい実施の形態について、図面を参照しながら説明する。
本発明に係る発電所の運転方法の第1の形態は、復水系統の構成材料に銅合金を使用しかつ全揮発性薬品処理を実施している発電所における運転方法であって、ヒドラジン以外のアルカリ薬品により復水浄化装置入口水のpHを9以上に調整することを特徴とする方法である。そこでまず、pHによる影響を、従来同様、ヒドラジンによるpH調整の場合について調べた。
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.
A first mode of a power plant operation method according to the present invention is a power plant operation method using a copper alloy as a constituent material of a condensate system and performing a total volatile chemical treatment, except for hydrazine. The pH of the condensate purification apparatus inlet water is adjusted to 9 or more with the above alkaline chemicals. Therefore, first, the effect of pH was examined in the case of pH adjustment with hydrazine as in the past.
ポリスルフォン素材の中空糸膜フィルタを以下の水質条件で通水し、物理的強度の経時変化を確認した。その結果、pHが高い(9以上の)水質条件ではポリスルフォン素材の中空糸膜フィルタにおける物理強度の低下は抑制されることが確認された。物理強度は、中空糸膜フィルタの引張伸度保持率で評価した。
水質条件:
ヒドラジン濃度:1000mg/L
銅イオン濃度 : 500mg/L
溶存酸素濃度 : 10μg/L
pH:8(図1に示すpHによる影響−1)
9(図2に示すpHによる影響−2)
A hollow fiber membrane filter made of polysulfone was passed through under the following water quality conditions, and changes in physical strength over time were confirmed. As a result, it was confirmed that a decrease in physical strength in the hollow fiber membrane filter made of polysulfone material was suppressed under water quality conditions having a high pH (9 or more). The physical strength was evaluated by the tensile elongation retention rate of the hollow fiber membrane filter.
Water quality conditions:
Hydrazine concentration: 1000mg / L
Copper ion concentration: 500mg / L
Dissolved oxygen concentration: 10μg / L
pH: 8 (Effect of pH shown in FIG. 1)
9 (Effect of pH shown in FIG. 2-2)
このように、pHを9以上に調整することにより、ポリスルフォン素材の中空糸膜フィルタの引張伸度保持率を高く維持できることが確認できたが、pH調整薬品として、ヒドラジンと、ヒドラジン以外のアルカリ薬品とでは、中空糸膜フィルタの引張伸度に関する影響度がどのように違うのかを調べるために、強制的な浸漬試験を行った。その測定結果を図3に示す。図3に示すように、ヒドラジン以外のアルカリ薬品に長時間接触(浸漬)させた場合には、ヒドラジンのみに長時間接触(浸漬)させる場合に比べて、引張伸度保持率を高く維持することができる(つまり、膜劣化の進行を抑えることができる)ことが分かった。 Thus, it was confirmed that by adjusting the pH to 9 or more, the tensile elongation retention rate of the hollow fiber membrane filter made of polysulfone material can be maintained high. However, as pH adjusting chemicals, hydrazine and alkalis other than hydrazine were used. In order to examine how the influence of the hollow fiber membrane filter on the tensile elongation differs from that of chemicals, a forced immersion test was conducted. The measurement results are shown in FIG. As shown in FIG. 3, the tensile elongation retention rate is maintained higher when contacted (immersed) with alkaline chemicals other than hydrazine for a long time than when contacted (immersed) with hydrazine alone for a long time. (That is, it is possible to suppress the progress of film deterioration).
そこで、ヒドラジン(N2 H4 )のみを添加した場合と(図4:図1の特性と実質的に同じで、少量のヒドラジン添加によりpHは8に調整されている)、さらにヒドラジン以外のアルカリ薬品を添加してpHを9以上に調整した場合(図5、図6)について、ポリスルフォン素材の中空糸膜フィルタの引張伸度保持率に及ぼす影響の比較試験を実施した。図5、図6から分かるように、ヒドラジン以外のアルカリ薬品(アンモニア(NH3 )およびエタノールアミン(ETA))による膜劣化の影響はなく、図3も加えて考慮すると、ヒドラジン単独の場合よりも劣化が緩和されることが確認された。 Therefore, when only hydrazine (N 2 H 4 ) is added (FIG. 4: substantially the same as the characteristics of FIG. 1, the pH is adjusted to 8 by adding a small amount of hydrazine), and an alkali other than hydrazine. When the pH was adjusted to 9 or more by adding a chemical (FIGS. 5 and 6), a comparative test of the influence of the polysulfone material on the tensile elongation retention rate of the hollow fiber membrane filter was performed. As can be seen from FIG. 5 and FIG. 6, there is no influence of film deterioration due to alkaline chemicals other than hydrazine (ammonia (NH 3 ) and ethanolamine (ETA)), and in addition to FIG. It was confirmed that the deterioration was alleviated.
このようなヒドラジン以外のアルカリ薬品は、例えば復水系統における復水クリーンアップ初期に添加されることが好ましく、後述の脱気純水を使用しない場合には、少なくとも系統内真空度上昇後、復水溶存酸素濃度(DO濃度)が1ppm以下となる時期まで添加することが好ましい。添加場所は特に限定されないが、復水系統中の復水器後段や復水脱塩装置後段での添加が例示できる。 Such alkaline chemicals other than hydrazine are preferably added, for example, at the initial stage of condensate cleanup in the condensate system. When degassed pure water described later is not used, at least after the vacuum level in the system is increased, It is preferable to add until the time when the water-soluble oxygen concentration (DO concentration) becomes 1 ppm or less. Although an addition place is not specifically limited, The addition in the back | latter stage of the condenser in a condensate system | strain and the back | latter stage of a condensate demineralizer can be illustrated.
本発明に係る発電所の運転方法の第2の形態は、復水系統の構成材料に銅合金を使用しかつ全揮発性薬品処理を実施している発電所における運転方法であって、復水浄化装置入口水の溶存酸素を1ppm以下に調整することを特徴とする方法である。そこで、ポリスルフォン素材の中空糸膜フィルタを図7に示す通水流速、水質条件で通水し、溶存酸素濃度と物理的強度の経時変化(引張伸度保持率)との関係を調べた。その結果、溶存酸素が1ppm以下の水質条件ではポリスルフォン素材の中空糸膜フィルタにおける物理的強度の低下は抑制されることが確認された。 A second form of operation method of a power plant according to the present invention is an operation method in a power plant that uses a copper alloy as a constituent material of a condensate system and performs total volatile chemical treatment. The method is characterized in that the dissolved oxygen in the purification apparatus inlet water is adjusted to 1 ppm or less. Therefore, a polysulfone-based hollow fiber membrane filter was passed under the water flow rate and water quality conditions shown in FIG. 7, and the relationship between dissolved oxygen concentration and physical strength over time (tensile elongation retention) was examined. As a result, it was confirmed that the decrease in physical strength of the hollow fiber membrane filter made of polysulfone material was suppressed under water quality conditions where the dissolved oxygen was 1 ppm or less.
この復水浄化装置入口水の溶存酸素を1ppm以下に調整するためには、例えば脱気純水を復水系統中に供給する方法や、復水系統および/または給水系統を窒素シールする方法などを採用できる。 In order to adjust the dissolved oxygen of the condensate purification apparatus inlet water to 1 ppm or less, for example, a method of supplying degassed pure water into the condensate system, a method of sealing the condensate system and / or the water supply system with nitrogen, etc. Can be adopted.
本発明に係る発電所の運転方法の第3の形態は、復水系統の構成材料に銅合金を使用しかつ全揮発性薬品処理を実施している発電所における運転方法であって、運転前に予め酸化鉄または/および水酸化鉄を復水浄化装置のろ過膜表面に捕捉させ、しかる後に通水処理を行うことを特徴とする方法である。そこで、ポリスルフォン素材の中空糸膜フィルタを図8に示す条件で通水する場合と、図9に示すように運転前に予め酸化鉄または/および水酸化鉄を復水浄化装置のろ過膜表面に捕捉させ、しかる後に通水処理を行うとの比較試験を行った。その結果、酸化鉄を通水前に予めろ過表面に捕捉させることにより、ポリスルフォン素材の中空糸膜フィルタにおける物理強度(引張伸度保持率)の低下は抑制されることが確認された。 A third mode of the operation method of the power plant according to the present invention is an operation method in a power plant that uses a copper alloy as a constituent material of the condensate system and performs total volatile chemical treatment, In this method, iron oxide and / or iron hydroxide is previously captured on the filtration membrane surface of the condensate purification apparatus, and then water passing treatment is performed. Therefore, in the case where water is passed through a hollow fiber membrane filter made of a polysulfone material under the conditions shown in FIG. 8, and as shown in FIG. 9, the surface of the filtration membrane of the condensate purification device is pre-treated with iron oxide or / and iron hydroxide before operation. A comparative test was conducted in which the water was trapped and then subjected to water treatment. As a result, it was confirmed that the decrease in physical strength (tensile elongation retention) in the hollow fiber membrane filter made of a polysulfone material was suppressed by preliminarily capturing iron oxide on the filtration surface before water flow.
なお、本発明に係る発電所の運転方法の上記第1、第2、第3の形態は、任意に2つ以上組み合わせることが可能である。 In addition, the said 1st, 2nd, 3rd form of the operating method of the power plant which concerns on this invention can be combined arbitrarily two or more.
本発明は、銅合金を用いた機器を使用している加圧水型原子力発電所や火力発電所の復水系統に用いて好適な発電所の運転方法である。 The present invention is a power plant operation method suitable for use in a condensate system of a pressurized water nuclear power plant or a thermal power plant using equipment using a copper alloy.
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Publication number | Priority date | Publication date | Assignee | Title |
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JPS63150504A (en) * | 1986-12-12 | 1988-06-23 | 株式会社日立製作所 | Water treatment equipment |
JPS6463003A (en) * | 1987-09-04 | 1989-03-09 | Hitachi Ltd | Filtration method for hollow yarn membrane filter |
JPH0259090A (en) * | 1988-08-24 | 1990-02-28 | Japan Organo Co Ltd | Method for filtering condensed water |
JPH105761A (en) * | 1996-06-21 | 1998-01-13 | Asahi Chem Ind Co Ltd | Purifying method of condensate |
JP2001318188A (en) * | 2000-05-10 | 2001-11-16 | Japan Organo Co Ltd | Condensate purification system and its operation method |
JP2002004810A (en) * | 2000-06-19 | 2002-01-09 | Japan Organo Co Ltd | Method of treating condensate |
JP2003053161A (en) * | 2001-06-05 | 2003-02-25 | Japan Organo Co Ltd | Method for cleaning hollow fiber membrane module |
JP2004108240A (en) * | 2002-09-18 | 2004-04-08 | Mitsubishi Heavy Ind Ltd | Power generation plant and power generation method |
-
2005
- 2005-12-12 JP JP2005357253A patent/JP2007160162A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63150504A (en) * | 1986-12-12 | 1988-06-23 | 株式会社日立製作所 | Water treatment equipment |
JPS6463003A (en) * | 1987-09-04 | 1989-03-09 | Hitachi Ltd | Filtration method for hollow yarn membrane filter |
JPH0259090A (en) * | 1988-08-24 | 1990-02-28 | Japan Organo Co Ltd | Method for filtering condensed water |
JPH105761A (en) * | 1996-06-21 | 1998-01-13 | Asahi Chem Ind Co Ltd | Purifying method of condensate |
JP2001318188A (en) * | 2000-05-10 | 2001-11-16 | Japan Organo Co Ltd | Condensate purification system and its operation method |
JP2002004810A (en) * | 2000-06-19 | 2002-01-09 | Japan Organo Co Ltd | Method of treating condensate |
JP2003053161A (en) * | 2001-06-05 | 2003-02-25 | Japan Organo Co Ltd | Method for cleaning hollow fiber membrane module |
JP2004108240A (en) * | 2002-09-18 | 2004-04-08 | Mitsubishi Heavy Ind Ltd | Power generation plant and power generation method |
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