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作 者:孙希贤 李新民[1] 李建华[1] 范业梅[1] 徐恒泳[1] 苏玉[1] 史克英[1] 徐国林[1] 黄仁才[2] 周佩珩[2] 刘金香[3]
机构地区:[1]哈尔滨师范大学化学系,哈尔滨150080 [2]上海石油化工总厂化工二厂研究所 [3]中国科学院大连化学物理研究所
出 处:《高等学校化学学报》1992年第10期1302-1306,共5页Chemical Journal of Chinese Universities
摘 要:研究了甲烷二氧化碳转化反应的热力学特性,计算了反应平衡常数及平衡组成,分析和确定了抑制积碳的生成条件,采用固定床流动和脉冲反应装置研究了Ni/Al_2O_3催化剂对甲烷二氧化碳转化的催化性能。The thermodynamic properties of the conversion of methane and carbon dioxide were studied.The equilibrium constant of the reaction and the theoretical distributions of products were calculated in order to determine the operating conditions needed to inhibit carbon deposition.The catalytic activity of the conversion of CH4 and CO2 into synthesis gas over Ni/Al2O3 catalyst was examined by using a fixed-bed flow apparatus.It is found that CH4 and CO2 over Ni/Al2O3-3 catalyst has reached the theoretical equilibrium conversions,and the synthesis gas also reached the theoretical yield.The results indicate that Ni/Al2O3-3 catalyst has a high activity,selectivity and stability.
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