Membranes Matter: Preventing Ammonia Crossover during Electrochemical Ammonia Synthesis.
Logan M WilderKeenan WyattChristopher A SkangosW Ellis KleinMakenzie R ParimuhaJaclyn L KatsirubasJames L YoungElisa M MillerPublished in: ACS applied energy materials (2024)
The electrochemical nitrogen and nitrate reduction reactions (E-NRR and E-NO 3 RR) promise to provide decentralized and fossil-fuel-free ammonia synthesis, and as a result, E-NRR and E-NO 3 RR research has surged in recent years. Membrane NH 3 /NH 4 + crossover during E-NRR and E-NO 3 RR decreases Faradaic efficiency and thus the overall yield. During catalyst evaluation, such unaccounted-for crossover results in measurement error. Herein, several commercially available membranes were screened and evaluated for use in ammonia-generating electrolyzers. NH 3 /NH 4 + crossover of the commonly used cation-exchange membrane (CEM) Nafion 212 was measured in an H-cell architecture and found to be significant. Interestingly, some anion exchange membranes (AEMs) show negligible NH 4 + crossover, addressing the problem of measurement error due to NH 4 + crossover. Further investigation of select membranes in a zero-gap gas diffusion electrode (GDE)-cell determines that most membranes show significant NH 3 crossover when the cell is in an open circuit. However, uptake and crossover of NH 3 are mitigated when -1.6 V is applied across the GDE-cell. The results of this study present AEMs as a useful alternative to CEMs for H-cell E-NRR and E-NO 3 RR electrolyzer studies and present critical insight into membrane crossover in zero-gap GDE-cell E-NRR and E-NO 3 RR electrolyzers.