文献类型：期刊文献

英文题名：Multi-scale modeling of isobutane alkylation with 2-butene using composite ionic liquids as catalyst

作者：Zheng, Weizhong[1];Li, Di[1];Sun, Weizhen[1];Zhao, Ling[1]

机构：[1]East China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China

年份：2018

卷号：186

起止页码：209

外文期刊名：CHEMICAL ENGINEERING SCIENCE

收录：;EI(收录号：20181905144027);WOS:【SCI-EXPANDED(收录号:WOS:000436773200019)】；

基金：The financial support by the National Natural Science Foundation of China (91434108) is gratefully acknowledged.

语种：英文

外文关键词：Multi-scale modeling; Isobutane alkylation; Ionic liquid; Molecular dynamic simulation

摘要：The alkylation kinetics of isobutane with 2-butene catalyzed by composite ionic liquid (CIL) was investigated with batch experiments. The optimized reaction time of CIL-catalyzed alkylation was found to be less than 30 s, much shorter than the traditional H2SO4-catalyzed one. Based on the carbonium ion mechanism, the kinetic model was further established, in which the concentration profiles of three groups of key components in alkylates with time can be well predicted, i.e. trimethylpentane (TMPs), dimethylhexanes (DMHs) and heavy ends (HEs). The rate constant related to the formation of TMPs in the CIL alkylation is more than two orders of magnitude larger than that in the H2SO4 alkylation. The enhancement of the rate constants for the CIL alkylation at the macroscopic scale can be ascribed into the higher solvation and diffusion of isobutane in the CIL at the microscopic scale, which is confirmed by the solvation free energy and diffusion coefficient calculation using molecular dynamics simulation. Hopefully, the multi-scale information in this work can bring novel insights into the understanding of CIL-catalyzed alkylation and further the design and optimization of this process. (C) 2018 Elsevier Ltd. All rights reserved.