CO residence time modulates multi-carbon formation rates in a zero-gap Cu based CO2 electrolyzer

被引:3
作者
Subramanian, Siddhartha [1 ]
Kok, Jesse [1 ]
Gholkar, Pratik [3 ]
Sajeev Kumar, Asvin [2 ]
van Montfort, Hugo-Pieter Iglesias [1 ]
Kortlever, Ruud [2 ]
Urakawa, Atsushi [3 ]
Dam, Bernard [1 ]
Burdyny, Thomas [1 ]
机构
[1] Delft Univ Technol, Fac Appl Sci, Dept Chem Engn, Mat Energy Convers & Storage MECS, Van der Maasweg 9, NL-2629 HZ Delft, Netherlands
[2] Delft Univ Technol, Fac Mech Maritime & Mat Engn, Proc & Energy Dept, Large Scale Energy Storage, NL-2628 CB Delft, Netherlands
[3] Delft Univ Technol, Dept Chem Engn, Catalysis Engn, van der Maasweg 9, NL-2629 HZ Delft, Netherlands
关键词
MEMBRANE FUEL-CELL; CARBON-MONOXIDE; ELECTROCHEMICAL REDUCTION; ELECTROREDUCTION; HYDROCARBONS; SELECTIVITY; CATALYSIS; PRODUCTS; COVERAGE; ETHYLENE;
D O I
10.1039/d4ee02004a
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Carbon dioxide (CO2) electrolysis on copper (Cu) catalysts has attracted interest due to its direct production of C2+ feedstocks. Using the knowledge that CO2 reduction on copper is primarily a tandem reaction of CO2 to CO and CO to C2+ products, we show that modulating CO concentrations within the liquid catalyst layer allows for a C2+ selectivity of >80% at 200 mA cm(-2) under broad conversion conditions. The importance of CO pooling is demonstrated through residence time distribution curves, varying flow fields (serpentine/parallel/interdigitated), and flow rates. While serpentine flow fields require high conversions to limit CO selectivity and maximize C2+ selectivity, the longer CO residence times of parallel flow fields achieve similar selectivity over broad flow rates. Critically, we show that parts of the catalyst area predominantly reduce CO instead of CO2 as supported by CO reduction experiments, transport modelling, and achieving a CO2 utilization efficiency greater than the theoretical limit of 25% for C2+ products.
引用
收藏
页码:6728 / 6738
页数:11
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