阳极
阴极
工艺工程
动力学
原材料
大规模运输
化学
过程(计算)
化学工程
环境科学
材料科学
生化工程
计算机科学
电极
工程类
物理化学
量子力学
操作系统
物理
有机化学
作者
Yuanxin Fang,Haozhe Cui,Bo Chen,Wanting Chen,Xuehua Ruan,Xuemei Wu,Fujun Cui,Minggang Guo,Gaohong He
标识
DOI:10.1016/j.ces.2022.117996
摘要
Modeling of CO2 electroreduction reactor (CO2ECR) is highly demanded for rapid design of industrial processes, while facing challenges in practical applications. Herein, a kinetics-mass transport model is proposed, which can well balance the competition between HCOO– produce and H2 evolution, and be easily integrated into Aspen HYSYS as a user defined module for CO2ECR process design. By considering both cathode potential and CO2 concentration in flow channel, optimal regions of the key parameters can be simulated to achieve high efficiency of CO2 electroreduction, i.e., about 80 % for both HCOO– Faraday efficiency and CO2 conversion with slightly compressed pure CO2 feedstock of 300 kPa. By increasing anode flow rates, the lean streams with H2 concentration of around 50% achieve nearly the maximum H2 utilization, which is attractive due to the possible reduction of purification cost.
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