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作 者:李佳蓉[1,2,3] 王强[1] 刘艺 周朝晖 LI Jia-rong;WANG Qiang;LIU Yi;ZHOU Zhao-hui(Department of Chemical Engineering,School of Water and Environment,Chang’an University,Xi’an 710054,China;Key Laboratory of Subsurface Hydrology and Ecological Effect in Arid Region of the Ministry of Education,Chang’an University,Xi’an 710054,China;Key Laboratory of Eco-Hydrology and Water Security in Arid and Semi-Arid Regions of Ministry of Water Resources,Chang’an University,Xi’an 710054,China)
机构地区:[1]长安大学水利与环境学院化工系,陕西西安710054 [2]长安大学旱区地下水文与生态效应教育部重点实验室,陕西西安710054 [3]长安大学水利部旱区生态水文与水安全重点实验室,陕西西安710054
出 处:《应用化工》2024年第3期565-568,共4页Applied Chemical Industry
基 金:陕西省自然科学基础研究计划一般项目(2019JQ-440);陕西省自然科学基金(2023-JC-QN-0618);长安大学中央高校基本科研业务费(300102293104)。
摘 要:通过扩大H型反应器,利用面积超过100 cm 2的铟金属片和锡金属片电极电催化还原二氧化碳制甲酸。从二氧化碳还原反应产物的选择性、电解能力等方面进行了研究,得到了大尺寸金属电极反应器电催化制甲酸的优化方法。结果表明,进气流量40 mL/min和电流密度-3.0~-4.5 mA/cm^(2)区间及中性电解质为反应的最佳条件。By enlarging the H-type reactor,formic acid is produced by electrocatalytic reduction of carbon dioxide using indium metal sheet and tin metal sheet electrodes with an area of more than 100 cm 2.The selectivity of carbon dioxide reduction reaction products,electrolysis ability and other aspects were studied,and the optimization method of electrocatalytic formic acid production in large-scale metal electrode reactor was obtained.The results show that the optimal conditions for the reaction are the air inlet flow rate of 40 mL/min,the current density of-3.0 to-4.5 mA/cm 2,and the neutral electrolyte.
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