Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures
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Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures
Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures
中国化学工程学报(英文版)2023年53卷第1期 页码:63-72
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Department of Chemical and Biochemical Engineering, College of Chemistry and Chemical Engineering, Xiamen University,Xiamen,China,361005
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纸质出版:2023
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Zhiwei Wang, Yu Zhang, Zhi Zhang, 等. Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures[J]. 中国化学工程学报(英文版), 2023,53(1):63-72.
Zhiwei Wang, Yu Zhang, Zhi Zhang, Daowei Zhou, Zhikai Cao, Yong Sha. Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures[J]. Chinese Journal of Chemical Engineering, 2023, 53(1): 63-72.
Zhiwei Wang, Yu Zhang, Zhi Zhang, 等. Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures[J]. 中国化学工程学报(英文版), 2023,53(1):63-72.DOI:
Zhiwei Wang, Yu Zhang, Zhi Zhang, Daowei Zhou, Zhikai Cao, Yong Sha. Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures[J]. Chinese Journal of Chemical Engineering, 2023, 53(1): 63-72.DOI:
Investigation on catalytic distillation for ethyl acetate production with different catalytic packing structures
The catalytic packing is the core component of the catalytic distillation
and how the catalyst exists in the packing has significant influence on the process. To investigate the effect of catalyst packings on the catalytic distillation process
the classical ethyl acetate reactive distillation system was utilized
and a supported catalytic packing (SCP) was prepared in comparison with the conventional tea-bag catalytic packing (TBP). Laboratory scale experiments showed that the ethyl acetate conversion of the SCP was superior to the TBP at a low catalyst loading. The effects of reaction kinetics
mass transfer performance and actual catalytic efficiency of the packings on this process were regarded as reasons and studied by combining the experiments and numerical simulation. Results suggested that the relatively immediate “
in-situ
separation” caused by the rapid reaction kinetics and better mass transfer performance of SCP may be a main reason for the difference of the conversion.
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相关作者
Han-Qiao Hu
Yue Zhang
Ming Fan
Yong Cai
Guang-Wen Chu
Liang-Liang Zhang
Anshi Hong
Zisheng Zhang
相关机构
Research Center of the Ministry of Education for High Gravity Engineering and Technology, Beijing University of Chemical Technology
Petrochemical Research Institute, China National Petroleum Corporation
State Key Laboratory of Organic-Inorganic Composites, Beijing University of Chemical Technology
School of Chemical Engineering and Technology, National Engineering Research Center of Distillation Technology, Collaborative Innovation Center of Chemical Science and Engineering (Tianjin), Tianjin University
Department of Chemical and Biological Engineering, University of Ottawa