电解
合成气
电解质
碳酸盐
升级
化学工程
电化学
废物管理
碳酸钾
聚合物电解质膜电解
化学
催化作用
工艺工程
材料科学
电极
计算机科学
工程类
有机化学
物理化学
操作系统
生物化学
作者
Yuguang Li,Geonhui Lee,Tiange Yuan,Ying Wang,Dae‐Hyun Nam,Ziyun Wang,F. Pelayo Garcı́a de Arquer,Yanwei Lum,Cao‐Thang Dinh,Oleksandr Voznyy,Edward H. Sargent
出处
期刊:
日期:2019-05-06
被引量:2
标识
DOI:10.26434/chemrxiv.8081777
摘要
The process of CO2 valorization – all the way from capture/concentration of CO2 to its electrochemical upgrade - requires significant inputs in each of the capture, upgrade, and separation steps. The gas-phase CO2 feed following the capture-and-release stage and into the CO2 electroreduction stage produce a large waste of CO2 (between 80 and 95% of CO2 is wasted due to carbonate formation or electrolyte crossover) that adds cost and energy consumption to the CO2 management aspect of the system. Here we report an electrolyzer that instead directly upgrades carbonate electrolyte from CO2 capture solution to syngas, achieving 100% carbon utilization across the system. A bipolar membrane is used to produce proton in situ, under applied potential, which facilitates CO2 releasing at the membrane:catalyst interface from the carbonate solution. Using an Ag catalyst, we generate pure syngas at a 3:1 H2:CO ratio, with no CO2 dilution at the gas outlet, at a current density of 150 mA/cm2, and achieve a full cell energy efficiency of 35%. The direct carbonate cell was stable under a continuous 145 h of catalytic operation at ca. 180 mA/cm2. The work demonstrates that coupling CO2 electrolysis directly with a CO2 capture system can accelerate the path towards viable CO2 conversion technologies.
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