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

被引:28
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
国家重点研发计划; 中国国家自然科学基金;
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
相关论文
共 32 条
[1]   Nexus between clean energy consumption, economic growth and CO2 emissions [J].
Cai, Yifei ;
Sam, Chung Yan ;
Chang, Tsangyao .
JOURNAL OF CLEANER PRODUCTION, 2018, 182 :1001-1011
[2]   Analysis of dual fluidized bed gasification integrated system with liquid fuel and electricity products [J].
Chen, Hao ;
Zhang, Xiangping ;
Wu, Bin ;
Bao, Di ;
Zhang, Suojiang ;
Li, Jianwei ;
Lin, Weigang .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (26) :11062-11071
[3]  
[陈嵩嵩 Chen Songsong], 2018, [过程工程学报, The Chinese Journal of Process Engineering], V18, P1307
[4]  
El-Halwagi MM, 2017, SUSTAINABLE DESIGN THROUGH PROCESS INTEGRATION: FUNDAMENTALS AND APPLICATIONS TO INDUSTRIAL POLLUTION PREVENTION, RESOURCE CONSERVATION, AND PROFITABILITY ENHANCEMENT, 2ND EDITION, P1, DOI 10.1016/B978-0-12-809823-3.00001-1
[5]   Experimental and modeling studies on a homogeneous reactive distillation system for dimethyl carbonate synthesis by transesterification [J].
Fang, YJ ;
Xiao, WD .
SEPARATION AND PURIFICATION TECHNOLOGY, 2004, 34 (1-3) :255-263
[6]   Dimethyl carbonate: a versatile reagent for a sustainable valorization of renewables [J].
Fiorani, G. ;
Perosa, A. ;
Selva, M. .
GREEN CHEMISTRY, 2018, 20 (02) :288-322
[7]   Zero-energy penalty carbon capture and utilization for liquid fuel and power cogeneration with chemical looping combustion [J].
He, Yangdong ;
Zhu, Lin ;
Li, Luling ;
Sun, Ling .
JOURNAL OF CLEANER PRODUCTION, 2019, 235 :34-43
[8]   Design and Control of Dimethyl Carbonate-Methanol Separation via Extractive Distillation in the Dimethyl Carbonate Reactive-Distillation Process [J].
Hsu, Kai-Yi ;
Hsiao, Yuan-Chang ;
Chien, I-Lung .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (02) :735-749
[9]   Dual-ionic liquid system: an efficient catalyst for chemical fixation of CO2 to cyclic carbonates under mild conditions [J].
Hu, Jiayin ;
Ma, Jun ;
Liu, Huizhen ;
Qian, Qingli ;
Xie, Chao ;
Han, Buxing .
GREEN CHEMISTRY, 2018, 20 (13) :2990-2994
[10]   Production of diethyl carbonate from ethylene carbonate and ethanol over supported fluoro-perovskite catalysts [J].
Iida, Hajime ;
Kawaguchi, Ryuhei ;
Okumura, Kazu .
CATALYSIS COMMUNICATIONS, 2018, 108 :7-11