估价
阳极
电合成
生物燃料
生物量(生态学)
电化学
阴极
碳纤维
化学反应工程
工艺工程
环境科学
废物管理
化学
材料科学
制浆造纸工业
电极
工程类
有机化学
催化作用
海洋学
物理化学
复合材料
复合数
地质学
作者
Faraz Montazersadgh,Hao Zhang,Anas Alkayal,Benjamin R. Buckley,Ben Kolosz,Bing Xu,Jin Xuan
标识
DOI:10.1007/s11705-020-1945-6
摘要
Abstract Utilizing CO 2 in an electro-chemical process and synthesizing value-added chemicals are amongst the few viable and scalable pathways in carbon capture and utilization technologies. CO 2 electro-reduction is also counted as one of the main options entailing less fossil fuel consumption and as a future electrical energy storage strategy. The current study aims at developing a new electrochemical platform to produce low-carbon e-biofuel through multifunctional electrosynthesis and integrated co-valorisation of biomass feedstocks with captured CO 2 . In this approach, CO 2 is reduced at the cathode to produce drop-in fuels (e.g., methanol) while value-added chemicals (e.g., selective oxidation of alcohols, aldehydes, carboxylic acids and amines/amides) are produced at the anode. In this work, a numerical model of a continuous-flow design considering various anodic and cathodic reactions was built to determine the most techno-economically feasible configurations from the aspects of energy efficiency, environment impact and economical values. The reactor design was then optimized via parametric analysis.
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