Abstract

Abstract In this study, an integrated process of dimethyl carbonate (DMC) and ethylene glycol (EG) production from biomass was proposed. The process was started from biomass gasification, CO 2 separation and CO 2 conversion to ethylene carbonate. DMC and EG were produced via transesterification using reactive distillation and extractive reaction. A variety of key parameters of each part was examined to optimize operating condition, which is focused on heat consumption. DMC and EG can achieve 99.5 % mole of purity. The overall production can sustain itself without any external heat sources by using biomass combustion, and all performance indicators were considered under the energy self-sufficient conditions. The ratio of biomass fed to the gasifier and the combustor was found to be 0.34:0.66 (under energy self-sufficient conditions) where the C, H and O atom efficiencies of the process achieved were 32.87, 48.96 and 37.72%, respectively. Since all energy was supplied by biomass itself, the process was considered as carbon neutral with a fraction of carbon dioxide fixation from biomass into chemicals of 0.24.

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