(437f) Harnessing Mass Transport to Optimize Ammonia Production during Electrochemical Nitrate Reduction
AIChE Annual Meeting
2021
2021 Annual Meeting
Catalysis and Reaction Engineering Division
Nitrogen Chemistry I: Nitrate Reduction
Wednesday, November 10, 2021 - 9:20am to 9:40am
We used a membrane-separated flow cell and titanium foil electrode to study the influence of mass transport (Fig. 1a). Considering the two serial interfaces in the working electrode chamber (electrode/electrolyte and electrolyte/membrane), different strategies are employed to enhance mass transport across them. Nitrate removal, ammonia N-selectivity and Faradaic efficiency are chosen as key performance metrics.
Cross-membrane ion transport resistance can significantly limit the total current density of electrochemical systems. We have found that pairing membrane type (proton vs. cation exchange membrane) with the primary charge carrier species in bulk electrolyte can improve total current density and nitrate removal (Fig. 1b). Meanwhile, the structure of the diffusion layer at the electrode/electrolyte interface is strongly impacted by bulk electrolyte flow rate, which can be utilized to tune nitrate removal and ammonia production. Interestingly, the dependence of nitrate selectivity on flow rate shows opposite trends in different co-existing cation concentrations (Fig. 1c). Continuum models will be applied to solve interfacial potential and concentration profiles to illustrate the underlying mechanisms.
As an underexplored topic, mass transport processes in electrochemical NO3RR are being systematically studied and will be engineered to optimize ammonia production from polluted waters.