Fig. 4: CO2RR performance of the functionalized Ag–Cu electrodes measured in MEA electrolyzers.
From: Improved electrochemical conversion of CO2 to multicarbon products by using molecular doping

a Relationship between the current and cell voltage relationship of pristine, C3-, C2N-, N3N- and N2SN- functionalized electrodes. The CO2RR electrolysis was operated using CO2 with a flow rate of 10 sccm, 0.1 M KHCO3 anolyte with a flow rate of 30 mL min−1. b Corresponding partial current density for the C2+ products. c Comparison of FEs for C2+ on the different Ag–Cu electrodes measured at full-cell potentials ranging between −3.5 and −4.8 V. d Evolution of the Faradaic efficiency for C2+ and H2 with the CO2 flow rate. e Evolution of the FEs and full-cell energy efficiency (EE) for C2+ as a function of specific current densities for C2+ on the N2SN- functionalized Ag–Cu electrode. The error bars represent the standard deviation of three independent samples measured under different current densities. f Comparison of the performance metrics of the MEA electrolyzers based on N2SN-functionalized Ag–Cu cathodes with literature benchmark. For each report, the plotted values are those corresponding to the longest duration test32, 65,66,67. The references are from refs. 32, 65, 66, and 67. g CO2RR performance of N2SN-Ag–Cu catalyst at a full-cell potential of −4.55 V and with a 10 sccm feed in CO2 over 100 h. The anolyte consisted in a 0.1 M KHCO3 solution with a flow rate of 30 ml min−1. The blue line represents the current recorded during the extended CO2RR experiment (primary y axis). Each orange, gray, green, and purple spheres represent the FEs for C2H4, H2, CO and C3H6 averaged from three independent measurements (secondary y axis). The error bars in a, b, c, and e represent the standard deviation of three independent measurements.