Preparation of Pd/γ-Al2O3/nickel foam monolithic catalyst and its performance for selective hydrogenation in a rotating packed bed reactor

被引:3
作者
Liao, Hai-Long
Wang, Bao-Ju
Liu, Ya-Zhao
Luo, Yong [1 ]
Wang, Jie-Xin
Chu, Guang-Wen
Chen, Jian-Feng [1 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Organ Inorgan Composites, Beijing 100029, Peoples R China
来源
CHINESE JOURNAL OF CHEMICAL ENGINEERING | 2022年 / 41卷
基金
中国国家自然科学基金;
关键词
Monolithic catalyst; Rotating packed bed reactor; Hydrogenation; Selectivity; MASS-TRANSFER; INTENSIFICATION;
D O I
10.1016/j.cjche.2021.08.026
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Selective hydrogenation plays an important role in chemical industries, yet its selectivity is usually limited by the mass transfer. In this work, the enhanced hydrogenation selectivity was achieved in a rotating packed bed (RPB) reactor with excellent mass transfer efficiency. Aiming to be used under the centrifugal filed, a monolithic catalyst Pd/gamma-Al2O3/nickel foam suiting for the shape and size of the rotor of RPB reactor was prepared by the electrophoretic deposition method. The mechanical strength of the catalyst can meet the requirement of high centrifugal force in the RPB. The hydrogenation selectivity in the RPB reactor using the 3-methyl-1-pentyn-3-ol hydrogenation system was 3-8 times higher than that in a stirred tank reactor under similar conditions. This work proves the feasibility of intensifying the selectivity of hydrogenation process in the RPB reactor. (C) 2021 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:311 / 319
页数:9
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