“…While half-cell and small scale electrochemical ammonia reactors have been investigated in detail, little focus has been FIGURE 2 | (A) Reported performance from selected studies (Kordali et al, 2000;Han et al, 2018;Qin et al, 2018;Yang et al, 2018;Cong et al, 2019;Tao et al, 2019;Nazemi et al, 2020;Wei et al, 2021) of faradaic efficiency and ammonia formation rate, (B) theoretical full cell potential for reported literature half-cell and relationship to ammonia formation rate [y-axis same as (A)] (C) schematic representation of cell potential calculation in impact of ammonia formation overpotential in V vs NHE (normal hydrogen electrode) where E t, H2O and E t,H2 represent the theoretical potential for a reaction generating ammonia from either water or hydrogen as the proton source while E cell,H2 and E cell,H2O represent the measured potential required for the full cell arrangement which has 'z V' overpotential. on the practical application and process integration of these units.…”