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KINETICS OF CATALYTIC STEAM REFORMING OF n—BUTANE

gradientless reactor.The reaction temperature was varied in the range of 743—853 K,and the steam to carbon molar ratio in the feed was 3,4 or 5

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Zircaloy Oxidation and Cladding Deformation in PWR-Specific

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KINETICS OF CATALYTIC STEAM REFORMING OF n—BUTANE

gradientless reactor.The reaction temperature was varied in the range of 743—853 K,and the steam to carbon molar ratio in the feed was 3,4 or 5

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743 853K.The molar ratio of steam to carbon was 3-5 in the feed.The experimental results show that methane,carbon monoxide,carbon dioxide and

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