Ion exchange (IX) is a promising
technology for selective nitrogen
recovery from urine; however, IX requires chemical-intensive regeneration
that escalates energy consumption and carbon emissions. To overcome
this barrier, we demonstrated and investigated a novel electrified
IX stripping process (EXS) enabling electrochemical in situ IX regeneration with simultaneous ammonia stripping. EXS combines
a weak acid cation exchange resin (WAC) to concentrate ammonia, a
bipolar membrane to produce protons for WAC regeneration, and membrane
stripping to recover the eluted ammonium from WAC. We observed over
80% regeneration (elution from resin) and recovery (membrane stripping)
efficiencies during multiple adsorption–recovery cycles with
synthetic and real urine. Comparing WAC with a strong acid cation
exchange resin illustrated the critical role of the proton affinity
of resin moieties in regulating resin regenerability and conductivity
in EXS, which we distinguished from the rationale for material choice
in electrodeionization. Compared to other electrochemical recovery
methods using unamended wastewater as an electrolyte, EXS enabled
control of electrolyte composition during recovery by separating and
equalizing influent ammonium via WAC-mediated removal. This electrolyte
engineering facilitated tunable EXS energy efficiency (100–300
MJ/kg N). This study informs the design of electrified, intensified
systems that enable decentralized nitrogen recovery from urine.