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首页> 外文期刊>Journal of the Japan Petroleum Institute >Propene Production from Ethene and Methane Using Silver- and Proton-exchanged Zeolite Catalysts
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Propene Production from Ethene and Methane Using Silver- and Proton-exchanged Zeolite Catalysts

机译:用银和质子交换的沸石催化剂从乙烯和甲烷生产丙烯

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摘要

Two new methods for the catalytic synthesis of propene using solid acid catalysts are presented. The first approach is a new method for the activation of methane, involving conversion of methane to propene over silver-exchanged zeolite in the presence of ethene. In the second method, ethene conversion proceeds directly and selectively over proton-exchanged zeolite under the control of a molecular sieving effect. The heterolytic dissociation of methane over silver cationic clusters (Ag_n~+) in Ag~+-exchanged zeolites, leading to the formation of silver hydride (Ag_n-H) and CH3~(δ+) species, which reacts with ethene to form propene around 673 K. Using ~(13)C-labeled methane as a reactant, propene is shown to be a primary product from methane and ethene. Thus, a significant proportion of propene was singly ~(13)C-labeled (~(13)CC2H6). Under these reaction conditions, H~+-exchanged zeolites, such as H-ZSM-5 do not catalyze the methane conversion, only ethene being converted into higher hydrocarbons, such as propene. Ethene is selectively converted to propene over SAPO-34 at 723 ?with a yield of 52.2% and selectivity of 73.3% at ethene conversion of 71.2%. The high and selective propene yields achieved over SAPO-34 can be attributed to a shape selectivity effect of the small-pore SAPO-34.
机译:提出了两种使用固体酸催化剂催化合成丙烯的新方法。第一种方法是用于甲烷活化的新方法,包括在乙烯存在下通过银交换沸石将甲烷转化为丙烯。在第二种方法中,在分子筛作用的控制下,乙烯的转化直接和选择性地超过了质子交换的沸石。甲烷在Ag_ +交换的沸石中的银阳离子簇(Ag_n〜+)上的杂化解离,导致形成氢化银(Ag_n-H)和CH3〜(δ+)物种,后者与乙烯反应形成丙烯大约673K。使用〜(13)C标记的甲烷作为反应物,表明丙烯是甲烷和乙烯的主要产物。因此,显着比例的丙烯单独被〜(13)C标记(〜(13)CC2H6)。在这些反应条件下,H +交换的沸石(例如H-ZSM-5)不会催化甲烷的转化,只有乙烯会转化为高级烃(例如丙烯)。乙炔在723℃下通过SAPO-34选择性地转化为丙烯,产率为52.2%,在乙烯转化率为71.2%时选择性为73.3%。通过SAPO-34获得的高选择性丙烯收率可归因于小孔SAPO-34的形状选择性作用。

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