Catalytic properties of benzene hydroxylation by TS-1 film reactor and Pd-TS-1 composite membrane reactor

被引：51

作者：

Wang, Xiaobin ^{[1
]}

Guo, Yu ^{[1
]}

Zhang, Xiongfu ^{[1
]}

Wang, Yao ^{[1
]}

Liu, Haiou ^{[1
]}

Wang, Jinqu ^{[1
]}

Qiu, Jieshan ^{[1
]}

Yeung, King Lun ^{[2
]}

机构：

[1] Dalian Univ Technol, Sch Chem Engn, State Key Lab Fine Chem, Dalian 116012, Liao Ning, Peoples R China

[2] Hong Kong Univ Sci & Technol, Dept Chem & Biomol Engn, Kowloon, Hong Kong, Peoples R China

来源：

CATALYSIS TODAY | 2010年 / 156卷 / 3-4期

基金：

中国国家自然科学基金;

关键词：

Film; Composite membrane; TS-1; Pd membrane; Catalytic membrane reactor; KNOEVENAGEL CONDENSATION REACTION; 1-PENTENE EPOXIDATION; PALLADIUM MEMBRANE; HYDROGEN-PEROXIDE; ZEOLITE; PHENOL; OXIDATION; OXYGEN; MICROSTRUCTURE; CHEMISTRY;

D O I：

10.1016/j.cattod.2010.03.034

中图分类号：

O69 [应用化学];

学科分类号：

081704 ;

摘要：

Titanium silicalite-1 (TS-1) and mesoporous TS-1p were incorporated as catalyst for the direct hydroxylation of benzene to phenol in a palladium membrane reactor. The zeolite also served as intermediate support layer and diffusion barrier against contaminants. Pd-TS-1 and Pd-TS-1p were characterized and tested for hydrogen permeation before investigating their performance for the benzene direct hydroxylation reaction. The effects of reactor configuration, reaction conditions and catalysts on conversion, product yield and water production were examined. The phenol yield of Pd-TS-1p was the highest followed by Pd-Sil-1 and Pd-TS-1 with Pd-TS-1p and Pd-TS-1 having phenol selectivity higher than 95%. The optimum reactor configuration and H-2/O-2 molar feed ratio were identified. (C) 2010 Elsevier B.V. All rights reserved.

引用

页码：288 / 294

页数：7

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