Kinetics measurement of ethylene-carbonate synthesis via a fast transesterification by microreactors
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Kinetics measurement of ethylene-carbonate synthesis via a fast transesterification by microreactors
Kinetics measurement of ethylene-carbonate synthesis via a fast transesterification by microreactors
中国化学工程学报(英文版)2023年53卷第1期 页码:243-250
Affiliations:
1. Engineering Research Center of Reactive Distillation, Fujian Province Higher Education Institutes, College of Chemical Engineering, Fuzhou University,Fuzhou,China,350108
Tengjie Wang, Wenkai Li, Xuehui Ge, 等. Kinetics measurement of ethylene-carbonate synthesis via a fast transesterification by microreactors[J]. 中国化学工程学报(英文版), 2023,53(1):243-250.
a fast transesterification by microreactors[J]. 中国化学工程学报, 2023, 53(1): 243-250.
Tengjie Wang, Wenkai Li, Xuehui Ge, 等. Kinetics measurement of ethylene-carbonate synthesis via a fast transesterification by microreactors[J]. 中国化学工程学报(英文版), 2023,53(1):243-250.DOI:
a fast transesterification by microreactors[J]. 中国化学工程学报, 2023, 53(1): 243-250.DOI:
Kinetics measurement of ethylene-carbonate synthesis via a fast transesterification by microreactors
High-purity ethylene carbonate (EC) is widely used as battery electrolyte
polycarbonate monomer
organic intermediate
and so on. An economical and sustainable route to synthesize high-purity ethylene carbonate (EC)
via
the transesterification of dimethyl carbonate (DMC) with ethylene glycol (EG) is provided in this work. However
this reaction is so fast that the reaction kinetics
which is essential for the industrial design
is hard to get by the traditional measuring method. In this work
an easy-to-assemble microreactor was used to precisely determine the reaction kinetics for the fast transesterification of DMC with EG using sodium methoxide as catalyst. The effects of flow rate
microreactor diameter
catalyst concentration
reaction temperature
and reactant molar ratio were investigated. An activity-based pseudo-homogeneous kinetic model
which considered the non-ideal properties of reaction system
was established to describe the transesterification of DMC with EG. Detailed kinetics data were collected in the first 5 min. Using these data
the parameters of the kinetic model were correlated with the maximum average error of 11.19%. Using this kinetic model
the kinetic data at different cataly
st concentrations and reactant molar ratios were predicted with the maximum average error of 13.68%
suggesting its satisfactory prediction performance.
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