Novel eco-efficient reactive distillation process for dimethyl carbonate production by indirect alcoholysis of urea  

作　　者：Iulian Patrașcu Costin S.Bîldea Anton A.Kiss 

机构地区：[1]Department of Chemical and Biochemical Engineering,University“Politehnica”of Bucharest,011061 Bucharest,Romania [2]Department of Chemical Engineering and Analytical Science,The University of Manchester,Manchester M139PL,UK

出　　处：《Frontiers of Chemical Science and Engineering》2022年第2期316-331,共16页化学科学与工程前沿（英文版）

基　　金：The financial support of the European Commission through the European Regional Development Fund and of the Romanian state budget,under the grant agreement POC P-37-449(acronym ASPiRE)is gratefully acknowledged;AAK gratefully acknowledges the Royal Society Wolfson Research Merit Award(Grant No.WM170003).

摘　　要：Dimethyl carbonate is an eco-friendly essential chemical that can be sustainably produced from CO_(2),which is available from carbon capture activities or can even be captured from the air.The rapid increase in dimethyl carbonate demand is driven by the fast growth of polycarbonates,solvent,pharmaceutical,and lithium-ion battery industries.Dimethyl carbonate can be produced from CO_(2)through various chemical pathways,but the most convenient route reported is the indirect alcoholysis of urea.Previous research used techniques such as heat integration and reactive distillation to reduce the energy use and costs,but the use of an excess of methanol in the trans-esterification step led to an energy intensive extractive distillation required to break the dimethyl carbonate-methanol azeotrope.This work shows that the production of dimethyl carbonate by indirect alcoholysis of urea can be improved by using an excess of propylene carbonate(instead of an excess of methanol),a neat feat that we showed it requires only 2.64 kW·h·kg^(-1) dimethyl carbonate in a reaction-separation-recycle process,and a reactive distillation column that effectively replaces two conventional distillation columns and the reactor for dimethyl carbonate synthesis.Therefore,less equipment is required,the methanol-dimethyl carbonate azeotrope does not need to be recycled,and the overall savings are higher.Moreover,we propose the use of a reactive distillation column in a heat integrated process to obtain high purity dimethyl carbonate(>99.8 wt-%).The energy requirement is reduced by heat integration to just 1.25 kW·h·kg^(-1) dimethyl carbonate,which is about 52%lower than the reaction-separation-recycle process.To benefit from the energy savings,the dynamics and control of the process are provided for10%changes in the nominal rate of 32 ktpy dimethyl carbonate,and for uncertainties in reaction kinetics.

关 键 词：dimethyl carbonate reactive distillation process design plantwide control 

分 类 号：O62[理学—有机化学]