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作 者:LuJiangyin ZhaoZhen XuChunming ZhangPu
机构地区:[1]StateKeyLaboratoryofHeavyOilProcessing,UniversityofPetroleum,Beijing102249,China
出 处:《Petroleum Science》2005年第1期52-56,共5页石油科学(英文版)
摘 要:Supported KVO3 catalysts were prepared by impregnating different kinds of supporters (α-Al2O3, γ-Al2O3 and SiO2 powders) with a KVO3 solution. The activity of the bare supporters and supported catalysts were evaluated in a continuous micro-reactivity test unit, with n-butane as a raw material. The results show that KVO3 has no catalytic activity, but it can increase the selectivity to light olefins. The supporter of α-Al2O3 has good catalytic performance for n-butane cracking when the reaction temperature is below 700℃.Supported KVO3 catalysts were prepared by impregnating different kinds of supporters (α-Al2O3, γ-Al2O3 and SiO2 powders) with a KVO3 solution. The activity of the bare supporters and supported catalysts were evaluated in a continuous micro-reactivity test unit, with n-butane as a raw material. The results show that KVO3 has no catalytic activity, but it can increase the selectivity to light olefins. The supporter of α-Al2O3 has good catalytic performance for n-butane cracking when the reaction temperature is below 700℃.
关 键 词:Catalytic cracking catalyst ALKENE N-BUTANE KVO3
分 类 号:TE626.88[石油与天然气工程—油气加工工程] TE624.41
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