Abstract

Recovering nitrogen from separately collected urine can potentially reduce cost and energy consumption of wastewater nitrogen removal and fertilizer production. In this study, we developed an open-loop hollow fiber membrane contactor (HFMC) to recover ammonium nitrogen from hydrolyzed human urine. Ammonia capture performance at various feed velocities and pH values was investigated. Be different from closed-loop HFMCs, the feed flow velocity is a vital operating parameter. The ammonia capture efficiency decreased from 80.13% to 33.06% when the feed flow velocity increased from 2.61 × 10−5 to 46.83 × 10−5 m s−1. Increasing feed pH from 10.0 to 12.0 enhanced ammonia capture efficiency from 62.12% to 80.13% by promoting the feed solution free ammonia fraction to increase the driving force. Ammonia mass transfer was investigated based on resistance-in-series model. Shell side mass transfer dominated the ammonia capture in the open-loop HFMC. The empirical shell side Sherwood correlation, Sh=17.4Dh1-φLRe0.6Sc0.33, fitted the experimental data well. The used polypropylene membrane showed good ion rejection performance with more than 99.44% rejection efficiency of PO43− and K+ which can be further recovered. The membrane also showed good stability during the ammonia capture experiments. The hydrophobicity, mechanical and pore properties did not significantly change.

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