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作 者:徐龙伢[1,2] 王昌东 贾继飞[1,2] 杨力 王德宝[1,2] 刘伟成 王清遐[1,2] 林励吾
机构地区:[1]中国科学院大连化学物理研究所催化基础国家重点实验室 [2]抚顺石化公司石油二厂
出 处:《催化学报》1998年第6期506-509,共4页
摘 要:乙烷与CO2的主要反应及其热力学研究表明,乙烷与CO2反应很复杂,提高CO2氧化乙烷脱氢生成乙烯的选择性,关键在于催化剂的开发;CO2不但可提高乙烷脱氢制乙烯的热力学平衡转化率,而且可与催化剂表面的积碳发生反应,延长催化剂的使用寿命.研究了催化剂上乙烷与CO2制乙烯反应的动力学,确定了CO2氧化乙烷脱氢反应的动力学方程及参数,表明乙烷与CO2制乙烯的反应速度比乙烷热裂解制乙烯的反应速度要大得多.The main reaction routes of C 2H 6 with CO 2 and their thermodynamics and kinetics were studied, which indicated that there are very complex reactions between C 2H 6 and CO 2. CO 2 can enhance the equilibrium conversion of thermodynamics for C 2H 4 formation from C 2H 6 dehydrogenation and can react with the surface deposited carbon, resulting in prolonging the life time of the catalyst. However, the exploration of the catalyst with desirable C 2H 4 selectivity from C 2H 6 dehydrogenation is the most important. In our studies, an M/Si 2 catalyst has been developed for C 2H 4 formation from C 2H 6 dehydrogenation with CO 2 as an oxidant. The parameters of kinetics equations for C 2H 4 formation from C 2H 6 and CO 2 were calculated and showed that the rate of C 2H 4 formation from C 2H 6 and CO 2 is greater than the that of C 2H 4 formation from C 2H 6 cracking process.
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