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Dehydrogenation of ethane to ethylene via radical pathways enhanced by alkali metal based catalyst in oxysteam condition

机译:氧蒸汽条件下,碱金属基催化剂通过自由基途径增强乙烷脱氢制乙烯

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The dehydrogenation of ethane to ethylene in the presence of oxygen and water was conducted using Na2WO4/SiO2 catalyst at high temperatures. At 923 K, the conversion rate without water was proportional to ethane pressure and a half order of oxygen pressure, consistent with a kinetically relevant step where an ethane molecule is activated with dissociated oxygen on the surface. When water was present, the ethane conversion rate was drastically enhanced. An additional term in the rate expression was proportional to a quarter of the oxygen pressure and a half order of the water pressure. This mechanism is consistent with the quasi-equilibrated OH radical formation with subsequent ethane activation. The attainable yield can be accurately described by taking the water contribution into consideration. At high conversion levels at 1073 K, the C2H4 yield exceeded 60 in a single-pass conversion. The C2H4 selectivity was almost insensitive to the C2H6 and O-2 pressures. (c) 2016 American Institute of Chemical Engineers AIChE J, 63: 105-110, 2017
机译:采用Na2WO4/SiO2催化剂在高温下对乙烷在氧气和水存在下进行脱氢制乙烯反应。在923 K时,没有水的转化率与乙烷压力和氧压的一半成正比,这与动力学相关步骤一致,其中乙烷分子在表面被解离的氧活化。当有水时,乙烷转化率大大提高。速率表达式中的附加项与氧压的四分之一和水压的二分之一成正比。该机理与随后乙烷活化的准平衡OH自由基形成一致。通过考虑水分贡献,可以准确描述可达到的产量。在 1073 K 的高转化水平下,C2H4 的单程转化率超过 60%。C2H4 选择性对 C2H6 和 O-2 压力几乎不敏感。(c) 2016 美国化学工程师学会 AIChE J, 63: 105-110, 2017

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