Recent research showed that the recovery of ammonia from simulated ammonium citrate scrubber effluent via bipolar membrane electrodialysis (BPMED) is less energy-intensive than from ammonium sulfate solutions. Nonetheless, the application of citric acid as scrubbing agent is limited by its high costs. This study aimed to improve BPMED performance for ammonium recovery using ammonium salts mixtures (ammonium sulfate and ammonium citrate) as feed solutions. Unlike previous studies that focused mainly on single-salt systems, it investigated how this combination affects ammonium recovery efficiency, current efficiency, energy consumption, ammonia diffusion, H⁺ and OH⁻ leakage to the diluate compartment, and anions transport across anion exchange membranes (AEMs) during BPMED. The ammonium recovery efficiency was higher for pure ammonium citrate (45.2 %) and mixture solutions (32.0–45.9 %) than for pure ammonium sulfate (26.8 %). Higher efficiency resulted from reduced competition between protons and ammonium across the cation exchange membrane (CEM). Feed with a higher ammonium citrate proportion increased buffer capacity, preventing protons leakage from the acid to the diluate compartment. This resulted in higher ammonium current efficiency for pure ammonium citrate (34.8 %) and mixture solutions (24.9–35.7 %) than for pure ammonium sulfate (20.4 %). The energy consumption was lower for pure ammonium citrate (14.1 kWh/kg-N recovered) and mixture solutions (13.0–17.4 kWh/kg-N recovered), than for pure ammonium sulfate (22.3 kWh/kg-N recovered). Ammonia diffusion from the base to the acid compartment reduced current efficiency by 19–23 % and accounted for 30–40 % of the total ammonium transported from the feed. This study demonstrated the effective use of ammonium citrate as one of the salts in the mixture to achieve high ammonium recovery efficiency with reduced energy consumption.