选择性
停留时间(流体动力学)
电解
催化作用
铜
化学
停留时间分布
二氧化碳
体积流量
碳纤维
化学工程
材料科学
无机化学
热力学
矿物学
物理化学
电极
电解质
有机化学
复合材料
物理
工程类
包裹体(矿物)
复合数
岩土工程
作者
Thomas Burdyny,Siddhartha Subramanian,Jonathan Kok,Pratik Gholkar,Asvin Sajeev Kumar,Hugo‐Pieter Iglesias van Montfort,Ruud Kortlever,Atsushi Urakawa,B. Dam
出处
期刊:Research Square - Research Square
日期:2023-11-09
被引量:1
标识
DOI:10.21203/rs.3.rs-3535552/v1
摘要
Abstract Carbon dioxide (CO 2 ) electrolysis on copper (Cu) catalysts has attracted interest for its direct production of C 2+ feedstocks. Using the knowledge that CO 2 reduction on copper is primarily a tandem reaction of CO 2 to CO and CO to C 2+ products, we show that modulating CO concentrations within the liquid catalyst layer allows for C 2+ selectivity of > 80 % at 200 mA cm ‑2 over broad conversion conditions. The importance of CO pooling is demonstrated through residence time distribution curves, varying flow fields (serpentine/parallel/interdigitated), and flow rate. While serpentine flow fields require high conversions to limit CO selectivity and maximize C 2+ selectivity, the longer CO residence times of parallel flow fields reach similar selectivity over broad flow rates. Critically, we show that parts of the catalyst area are predominantly reducing CO instead of CO 2 as supported by CO reduction experiments, transport modelling, and achieving a CO 2 utilization efficiency greater than the theoretical limit of 25 % for C 2+ products.
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