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Preparation of Highly Active Pt-K/γ-Al_2O_3 Catalyst for o-Phenylphenol Synthesis from o-Cyclohexenyl-cyclohexanone Dehydrogenation

Preparation of Highly Active Pt-K/γ-Al_2O_3 Catalyst for o-Phenylphenol Synthesis from o-Cyclohexenyl-cyclohexanone Dehydrogenation

作     者:DING Jie-lian LIN Ling XU Jian-dong ZENG Chong-yu 

作者机构:College of Chemistry and Chemical Engineering Nanjing University of Technology Nanjing 210009 P R. China 

出 版 物:《Chemical Research in Chinese Universities》 (高等学校化学研究(英文版))

年 卷 期:2008年第24卷第6期

页      面:726-730页

核心收录:

学科分类:07[理学] 0703[理学-化学] 

基  金:Supported by the Significant Technology Achievement Transformation Foundation of Jiangsu Province  China (No.Da2005043) 

主  题:o-Phenylphenol Pt catalyst K promoters Calcinations Reduction 

摘      要:0.5%Pt-K/γ-Al2O3 catalysts for the synthesis of o-phenylphenol(OPP) from o-cyclohexenyl-cyclohexanone (dimer) dehydrogenation were prepared by means of a two subsequent impregnation method. The effects of catalyst preparation parameters, such as K promoters, calcination, and reduction conditions, were investigated. The results showed that the addition of K2SO4 to Pt/γ-Al2O3 catalyst notably promoted the selectivity of OPP, and its optimum content was found to be 6% in mass fraction. The higher activity was obtained when Pt/γ-Al2O3 catalyst was calcined in nitrogen atmosphere at 400--500 ℃ and then reduced at the same temperature for 3 h in hydrogen atmosphere. The conversion of the dimer and the selectivity of OPP were always above 99% and 90%, respectively, over 0.5%Pt-6% K2SO4/γ-Al2O3 catalyst during the pilot scale test of 8000 h.

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