水素製造用の二基二循環方式を大循環システムに変更した場合、圧力変動を最も抑えるにはどうすればよいか？？
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水素製造用の二基二循環方式を大循環システムに変更した場合、圧力変動を最も抑えるにはどうすればよいか？？
精製、変換システムの圧力、一次吸気圧は同等に保ち、変更時は負荷を急に増減させず、ゆっくりと操作すること
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