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Kinetic limit of C_2 hydrocarbons yield at gas-phase oxidative coupling of methane

机译:甲烷气相氧化偶联C_2烃产率的动力学极限

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Oxidative coupling of methane into ethane and ethylene (OCM) is believed to be one of the most promising routes for methane conversion into more valuable products. Usually OCM is accomplished at atmospheric pressure and temperatures T=900-1200K with a use of catalysts. However, the highest yields of C_2 hydrocarbons that were reached so far are less the 25-30 percent due to a sharp decrease in selectivity of formation of C_2 hydrocarbons with the rise of oxygen content in reacting mixture. These yields are insufficient for the practical realisation of this technology. Many efforts to find appropriate catalysts to improve the process were made recently. According to the widely accepted mechanism of catalytic OCM, interaction of oxygen with surface of the catalyst leads to active centres, which dissociate molecules of methane to hydrogen atom and methyl radical. The formation of C_2 hydrocarbons takes place in subsequent gas-phase reactions. Such a mechanism of catalytic OCM may be compared with the gas-phase OCM mechanism with additional source of methyl radicals.
机译:甲烷氧化成乙烷和乙烯(OCM)的氧化偶联被认为是甲烷转化为更有价值产品中最有前途的途径之一。通常OCM在大气压和温度下以使用催化剂来完成。然而,到目前为止达到的最高产量的C_2烃的产量较小,因此由于C_2烃的形成性与反应混合物中的氧含量的升高而急剧下降,因此由于C_2烃的选择性急剧下降而较小。这些产量不足以实现这项技术的实际实现。最近努力寻找适当的催化剂来改善该过程。根据催化OCM的广泛接受机制,氧气与催化剂表面的相互作用导致活性中心,其将甲烷分散到氢原子和甲基。在随后的气相反应中形成C_2烃的形成。可以将这种催化OCM的机制与具有额外甲基源的气相OCM机制进行比较。

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