Cycloaddition of Biogas-Contained CO2 into Epoxides via Ionic Polymer Catalysis: An Experimental and Process Simulation Study

被引:2
作者
Hu, Xutao [1 ,2 ]
Bobbink, Felix D. [1 ]
van Muyden, Antoine [1 ]
Amiri, Masoud Talebi [3 ]
Bonnin, Alexy [1 ]
Marechal, Francois [3 ]
Nazeeruddin, Mohammad K. [4 ]
Qi, Zhiwen [2 ]
Dyson, Paul J. [1 ]
机构
[1] Ecole Polytech Fed Lausanne EPFL, Inst Sci & Ingn Chim, CH-1015 Lausanne, Switzerland
[2] East China Univ Sci & Technol, Max Planck Partner Grp, Sch Chem Engn, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
[3] Ecole Polytech Fed Lausanne EPFL, Ind Proc & Energy Syst Engn IPESE, CH-1951 Sion, Switzerland
[4] Ecole Polytech Fed Lausanne EPFL, Fac Basic Sci, Grp Mol Engn Funct Mat GMF, Inst Chem Sci & Engn, CH-1015 Lausanne, Switzerland
关键词
CARBON-DIOXIDE; CYCLIC CARBONATES; CAPTURE; ENERGY; OXIDE;
D O I
10.1021/acs.iecr.1c03895
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Biogas upgrading technologies are crucial for the production of high-purity biomethane. Efficient CO2 removal methods that are currently commercialized rely on "catch-and-release" mechanisms, and the CO2 stream is usually discharged into the atmosphere without further utilization. From the standpoint of process sustainability, it would be advantageous to transform the CO2 in biogas streams into value-added products. Herein, we propose the cycloaddition of CO2 into epoxides as a biogas upgrader. Fed by propylene oxide (PO) and biogas with typical CO2 concentration, or CO2 separated from biogas following upgrading, reactions were conducted under optimal conditions using an ionic polymer as the catalyst. Based on the obtained PO conversions, process simulations were performed for the large-scale production of propylene carbonate (PC) using CO2 separated from biogas. The PC yield was improved to 99.9% by process optimizations and reactant recycling at a molar flow rate of 100 kmol/h, which was shown to be commercially viable.
引用
收藏
页码:17942 / 17948
页数:7
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