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正丁烷在SO42-/ZrO2-Al2O3催化剂与H-USY分子筛上的异构化反应研究

Study on n-butane isomerization over SO42-/ZrO2-Al2O3 catalyst and H-USY zeolite

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【作者】 张文芳王鹏照杨朝合李春义

【Author】 ZHANG Wen-fang;WANG Peng-zhao;YANG Chao-he;LI Chun-yi;State Key Laboratory of Heavy Oil Processing,China University of Pertroleum ( East China);National Engineering Research Center of Chemical Fertilizer Catalyst,Fuzhou University;

【通讯作者】 李春义;

【机构】 中国石油大学(华东)重质油国家重点实验室福州大学化肥催化剂国家工程研究中心

【摘要】 对比了SO42-/Zr O2-Al2O3(SZA)催化剂和H-USY分子筛的物性结构,并在固定床微型反应装置上考察了2种催化剂酸性质对正丁烷异构化反应的影响。结果表明:H-USY分子筛的比表面积和孔体积明显高于SZA催化剂;SZA催化剂在150~250℃可催化正丁烷发生异构化反应,并以单分子反应为主,而H-USY分子筛在350~450℃才能催化正丁烷发生异构化反应,且单/双分子反应机理并存;SZA催化剂的失活速率明显大于H-USY分子筛,但其表面积炭量少于H-USY分子筛。

【Abstract】 The physical structures of SO42-/Zr O2-Al2O3(SZA)catalyst and H-USY zeolite were comparatively studied,and the effects of acid properties of two catalysts on properties of n-butane isomerization were investigated on a fixed bed micro-reactor.The results showed that the specific surface area and pore volume of H-USY zeolite were obviously larger than those of SZA catalyst;SZA catalyst at 150-250℃ could catalyze n-butane resulting in isomerization,mainly in monomolecular,while H-USY zeolite at 350-450℃ could catalyze n-butane leading to isomerization,and the reaction mechanisms of monomolecular and bimolecular coexisted.Furthermore,SZA catalyst with lower amount of coke deposits had higher deactivation rate,compared with that of H-USY zeolite.

【基金】 中国石油大学(华东)研究生自主创新工程基金资助项目(项目编号:YCX 2018036)
  • 【文献出处】 石化技术与应用 ,Petrochemical Technology & Application , 编辑部邮箱 ,2019年01期
  • 【分类号】O621.251
  • 【下载频次】143
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