“…Thecell operates at 20 8 8Cand atmospheric pressure.With respect to the cell reported by Kordali et al [8] we may note two main differences:1 )ino ur cell, the half-cell where the reduction of N 2 to NH 3 occurs,o perates in the gas-phase (electrolyte-less conditions;w ea lready demonstrated the feasibility and advantages of this approach for CO 2 conversion [14] ), while the cell of Kordali et al [8] operates in the presence of al iquid electrolyte;2 )these authors used a2m KOHa queous solution as the electrolyte,w hich shows limits when N 2 is replaced by air as CO 2 in air may react with KOHt of orm K 2 CO 3 .I na ddition, often stability of the electrodes is low under these strong basic conditions.The cell presented in Figure 1operates instead with adiluted concentration of KHCO 3 (only in the half-cell for water electrolysis, while electrolyte-less conditions are present in the cathode half-cell, where the reduction of N 2 to NH 3 occurs.I nt hese conditions,d on ot exists the problem of formation of potassium-carbonate by reaction with CO 2 .I ts hould be also commented that stronger basic conditions in the half-cell for water electrolysis enhance the reaction rate,but typically also lower the stability.F or this reason, we used adiluted aqueous solution of KHCO 3 ,j ust necessary to have enough conductivity.The half-cell, in which ammonia is synthetized, operates with ac ontinuous flow of the reactants.T his cell scheme allows an easy recovery of ammonia from the gas stream leaving the cell.…”