催化作用
电催化剂
电解
合成气
法拉第效率
碳酸盐
化学工程
纳米孔
电解水
化学
碳纤维
纳米技术
材料科学
电化学
有机化学
电解质
物理化学
电极
复合材料
复合数
工程类
作者
Hengzhou Liu,Lun An,Peiyao Wang,Christine Yu,Jie Zhang,Heejong Shin,Bosi Peng,Jiantao Li,Matthew Li,Hongmin An,Jiaqi Yu,Yuanjun Chen,Peiying Wang,Kug‐Seung Lee,Kanika Lalit,Zeyan Liu,Omar K. Farha,Wenyu Huang,Jefferson Zhe Liu,Long Qi
标识
DOI:10.1038/s41467-025-61407-8
摘要
Abstract Systems that sequentially capture and upgrade CO 2 from air to fuels/fuel-intermediates, such as syngas and ethylene, rely on an energy-intensive CO 2 release process. Electrified reactive capture systems transform CO 2 obtained directly from carbonate capture liquid into products. Previous reactive capture systems show a decline in Faradaic efficiencies (FE) at current densities above 200 mA/cm 2 . Here we show the chemical origins of this problem, finding that prior electrocatalyst designs failed to arrest, activate, and reduce in situ-generated CO 2 ( i -CO 2 ) before it traversed the catalyst layer and entered the tailgas stream. We develop a templated synthesis to define pore structures and the sites of Ni single atoms, and find that carbon-nitrogen-based nanopores are effective in accumulating i -CO 2 via short-range, non-electrostatic interactions between CO 2 molecules and the nanochannel walls. These interactions confine and enrich i -CO 2 within the pores, enhancing its binding and activation. We report as a result carbonate electrolysis at 300 mA/cm 2 with FE to CO of 50% ± 3%, and with <1% CO 2 in the tailgas outlet stream. This corresponds to a projected energy efficiency (EE) to 2:1 syngas of 46% at 300 mA/cm 2 when H 2 is added using a water electrolyzer.
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