Oloman Colin, Li Hui
Department of Chemical and Biological Engineering, University of British Columbia, 2360 East Mall, Vancouver, B.C. V6T 1Z3, Canada.
ChemSusChem. 2008;1(5):385-91. doi: 10.1002/cssc.200800015.
With respect to the negative role of carbon dioxide on our climate, it is clear that the time is ripe for the development of processes that convert CO(2) into useful products. The electroreduction of CO(2) is a prime candidate here, as the reaction at near-ambient conditions can yield organics such as formic acid, methanol, and methane. Recent laboratory work on the 100 A scale has shown that reduction of CO(2) to formate (HCO(2)(-)) may be carried out in a trickle-bed continuous electrochemical reactor under industrially viable conditions. Presuming the problems of cathode stability and formate crossover can be overcome, this type of reactor is proposed as the basis for a commercial operation. The viability of corresponding processes for electrosynthesis of formate salts and/or formic acid from CO(2) is examined here through conceptual flowsheets for two process options, each converting CO(2) at the rate of 100 tonnes per day.
关于二氧化碳对我们气候的负面作用,显然开发将二氧化碳转化为有用产品的工艺的时机已经成熟。二氧化碳的电还原是这里的主要候选方法,因为在接近环境条件下的反应可以产生甲酸、甲醇和甲烷等有机物。最近在100安培规模上的实验室工作表明,在工业可行的条件下,可以在滴流床连续电化学反应器中将二氧化碳还原为甲酸盐(HCO₂⁻)。假定阴极稳定性和甲酸盐渗透问题能够得到克服,这种类型的反应器被提议作为商业运营的基础。本文通过两种工艺方案的概念流程图来研究从二氧化碳电合成甲酸盐和/或甲酸的相应工艺的可行性,每种方案每天转化二氧化碳的速率为100吨。