Vapor phase ortho-selective alkylation of phenol with methanol over silica-manganese mixed oxide catalysts

被引:27
作者
Wang, Yanli [1 ]
Song, Yingying [1 ]
Huo, Weitao [2 ]
Jia, Mingjun [2 ]
Jing, Xiaoyan [1 ]
Yang, Piaoping [1 ]
Yang, Zhi [1 ]
Liu, Gang [2 ]
Zhang, Wenxiang [2 ]
机构
[1] Harbin Engn Univ, Coll Mat Sci & Chem Engn, Harbin 150001, Peoples R China
[2] Jilin Univ, State Key Lab Theoret & Computat Chem, Coll Chem, Changchun 130021, Peoples R China
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
Phenol alkylation; Manganese; o-Cresol; 2,6-Xylenol; ACID-BASE; METHYLATION; MN; COMBUSTION; OXIDATION; SITES; CO; ISOPROPYLATION; CU1-XCOXFE2O4; PYRIDINE;
D O I
10.1016/j.cej.2011.12.029
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The gas phase catalytic alkylation of phenol with methanol was investigated over a series of silica-manganese mixed oxide catalysts. The molar ratio of Si/Mn, the calcination temperature and the reaction temperature have considerable effect on the catalytic performance of the catalysts. All the Si-Mn mixed oxides are the active catalysts for the selective production of o-cresol and 2,6-xylenol. Among them, the catalyst with Si/Mn = 0.02, which is calcined at 773 K, shows the highest catalytic activity and selectivity to 2,6-xylenol. The existence of suitable Lewis acidic sites and/or basic sites might be responsible for the high activity and the ortho-selectivity of Si-Mn mixed oxides. During the reaction course, the partial reduction of Mn2O3/Mn3O4 can result in the decrease of Lewis acidity strength, which might be the main reason for the decrease of the selectivity to 2.6-xylenol. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:630 / 635
页数:6
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