大规模运输
电化学
电解质
吸收(声学)
化学工程
析氧
材料科学
催化作用
碳纤维
氧气
氧化还原
图层(电子)
扩散
传质
多孔性
扩散层
反应速率
电极
化学
分析化学(期刊)
氧气输送
无机化学
氧还原反应
还原(数学)
作者
Zhou Yu,Peng Zhu,Christina Bencin,Yuge Feng,Junwei Zhang,Zhiwei Fang,Shaoyun Hao,Ziang Xu,Chang Qiu,Ahmad Elgazzar,Sushanth Ashokkumar,Juan Wang,Haotian Wang
标识
DOI:10.1021/acsenergylett.5c04245
摘要
Electrochemical carbon capture based on an interfacial high-pH microenvironment represents a significant advancement in carbon capture technologies; however, its design remains constrained by limited carbon mass diffusion within the ultrathin catalyst layer, particularly in direct air capture (DAC) applications. Here, we demonstrated a practical approach to enhance interfacial CO2 mass transport through the implementation of an extended absorption layer (EAL) design. By incorporating the EAL into a porous solid electrolyte (PSE) reactor performing oxygen reduction reaction (ORR) and oxygen evolution reaction (OER) redox electrolysis, we achieved a seven-fold increase in both electron efficiency (10 mA cm–2, 28%) and CO2 capture rate (0.7 × 10–3 mL s–1 cm–2) for the DAC process. Stable operation of more than 35 days and continuous production of near-saturated carbonated water solely from indoor air were demonstrated in our device, indicating its practical applicability.
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