Investigation of Pd membrane reactors for one-step hydroxylation of benzene to phenol

被引:25
|
作者
Wang, Xiaobin [1 ,4 ]
Zhang, Xiongfu [1 ]
Liu, Haiou [1 ]
Qiu, Jieshan [1 ]
Han, Wei [2 ,3 ]
Yeung, King Lun [2 ,3 ]
机构
[1] Dalian Univ Technol, State Key Lab Fine Chem, Sch Chem Engn, Dalian 116024, Peoples R China
[2] Hong Kong Univ Sci & Technol, Dept Chem & Biomol Engn, Kowloon, Hong Kong, Peoples R China
[3] Hong Kong Univ Sci & Technol, Div Environm, Kowloon, Hong Kong, Peoples R China
[4] Shandong Univ Technol, Sch Chem Engn, Zibo 255049, Peoples R China
基金
中国国家自然科学基金;
关键词
Palladium membrane; Benzene hydroxylation; Catalytic membrane reactor; Phenol; SCANNING-TUNNELING-MICROSCOPY; POROUS STAINLESS-STEEL; PALLADIUM MEMBRANE; COMPOSITE MEMBRANES; 1-PENTENE EPOXIDATION; CATALYTIC-PROPERTIES; TS-1; ZEOLITE; OXIDATION; PERFORMANCE; HYDROGEN;
D O I
10.1016/j.cattod.2012.05.016
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Pd membrane reactor for one-step hydroxylation of benzene to phenol was investigated in an effort to reconcile the contradicting reports in the literature. A systematic study of the membrane, reactor and feed mode was conducted. Reactions carried out on Pd-TS-1 and Pd capillary membranes support Niwa's postulate of in situ hydrogen peroxide formation, but at the same time indicate that reactive species generated by reactions between permeated hydride ions and activated oxygen also participate in the reaction. The former reaction is important at low benzene feed concentrations and for reactors with small membrane area-to-reactor volume ratios. TS-1 catalyst in Pd-TS-1 membrane can significantly improve the yield and selectivity to phenol. High benzene feed concentrations and faster mass transfer gives the reactive species greater opportunity to react directly with benzene resulting in high benzene conversion but poor selectivity. (c) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:151 / 157
页数:7
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