A Study of the Catalytic Partial Oxidation of Hydrocarbons. XI. The Catalytic Activity of the MoO<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> and the MoO<SUB>3</SUB>–Bi<SUB>2</SUB>O<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> in the Selective Oxidation of Butene, B
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概要
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In the present work, the vapor-phase partial oxidation of <I>cis</I>-2-butene, butadiene, furan, and maleic anhydride was carried out over MoO<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> (1 : 0.2 atomic ratio) and MoO<SUB>3</SUB>–Bi<SUB>2</SUB>O<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> (1 : 1 : 0.2) with a contact time of 1.6 sec, at a concentration of 0.6–1.0%, and in air, in order to elucidate the difference between the two catalysts in their catalytic specificity for the oxidation of these reactants to maleic anhydride. Over the MoO<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> catalyst, the selectivities of butene, butadiene, and furan to maleic anhydride were 13, 50, and 78% respectively. Over the MoO<SUB>3</SUB>–Bi<SUB>2</SUB>O<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> catalyst, the formation of maleic anhydride from the reactants was very small, that of CO<SUB>2</SUB> was important, and the rate of maleic anhydride destruction was fairly high. It is considered that the MoO<SUB>3</SUB>–Bi<SUB>2</SUB>O<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> catalyst has almost the same catalytic specificity as the MoO<SUB>3</SUB>–P<SUB>2</SUB>O<SUB>5</SUB> in the C<SUB>4</SUB>H<SUB>8</SUB>→C<SUB>4</SUB>H<SUB>2</SUB>O<SUB>3</SUB> step, but that its activity for maleic anhydride destruction is so high that maleic anhydride cannot be accumulated.
- 公益社団法人 日本化学会の論文
著者
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Ai Mamoru
Research Laboratory Of Resources Utilization Tokyo Institute Of Technology
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Suzuki Sadao
Research Laboratory of Resources Utilization, Tokyo Institute of Technology
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