Recovery of ammonium nitrogen from human urine by an open-loop hollow fiber membrane contactor

被引:43
作者
Zhang, Junhui [1 ,2 ]
Xie, Mengfei [1 ,2 ]
Tong, Xin [3 ]
Liu, Su [3 ]
Qu, Dan [1 ,2 ,3 ]
Xiao, Shuhu [4 ]
机构
[1] Beijing Forestry Univ, Beijing Key Lab Source Control Technol Water Poll, 35 Qinghua East Rd, Beijing 100083, Peoples R China
[2] Beijing Forestry Univ, Coll Environm Sci & Engn, 35 Qinghua East Rd, Beijing 100083, Peoples R China
[3] Georgia Inst Technol, Brook Byers Inst Sustainable Syst, Atlanta, GA 30308 USA
[4] Chinese Res Inst Environm Sci, State Key Lab Environm Criteria & Risk Assessment, Beijing 100012, Peoples R China
基金
中国国家自然科学基金;
关键词
Ammonia capture; Source-separated urine; Hollow fiber membrane contactor; Open-loop; Mass transfer; POTASSIUM-PHOSPHATE-HEXAHYDRATE; SOURCE-SEPARATED URINE; WASTE-WATER; STRUVITE PRECIPITATION; SOLVENT-EXTRACTION; MASS-TRANSFER; REMOVAL; PHOSPHORUS; CRYSTALLIZATION; THERMODYNAMICS;
D O I
10.1016/j.seppur.2020.116579
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
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 x 10(-5) to 46.83 x 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 = 17.4 [D-h(1-phi)/L](ReSc0.33)-Sc-0.6, 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.
引用
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页数:10
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