Technical-environmental assessment of CO2 conversion process to dimethyl carbonate/ethylene glycol

被引:25
|
作者
Gu, Xincheng [1 ,3 ]
Zhang, Xiaochun [1 ]
Yang, Zifeng [1 ]
Shen, Weifeng [4 ]
Deng, Chun [3 ]
Zeng, Shaojuan [1 ]
Zhang, Xiangping [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing Key Lab Ion Liquids Clean Proc, Beijing 100190, Peoples R China
[2] Dalian Natl Lab Clean Energy, Dalian 116023, Peoples R China
[3] China Univ Petr, Coll Chem Engn, China State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[4] Chongqing Univ, Sch Chem & Chem Engn, Chongqing 400044, Peoples R China
基金
中国国家自然科学基金; 国家重点研发计划;
关键词
CO2; conversion; Dimethyl carbonate; Green degree; Process assessment; Process simulation; CYCLIC CARBONATES; IONIC LIQUIDS; ETHYLENE; SYSTEM; FUEL; DISTILLATION; FIXATION; DMC;
D O I
10.1016/j.jclepro.2020.125598
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Utilization of CO2 to produce value-added chemicals is a promising approach to mitigate greenhouse gas emissions. In this work, a new process for the conversion of CO2 to dimethyl carbonate (DMC) and ethylene glycol (EG) was rigorously simulated and assessed in term of the technical performance and the environmental impact. The proposed model involves the conversion of CO2 catalyzed by ionic liquid-based catalysts, the reactive distillation with the reaction kinetics model, the pressure-swing distillation with rigorous phase equilibrium equations, and complex material-energy nexus between each unit. The results show that the carbon utilization efficiency of this process reaches 99% and the negative CO2 emission is 0.14 ton CO2/ton product achieving CO2 reduction. The green degree value of the entire process is 176.30 gd/h indicating that this new process can be evaluated as an environmental friendly process. Additionally, the retrofitted heat exchanger network designed via the pinch technique achieves 48.70% saving in heating utility consumption and increasing the green degree by 193.89 gd/h. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页数:10
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