Pulsed electric field drives chemical-free membrane stripping for high ammonia recovery from urine

被引:8
|
作者
He, Jiazhou [1 ]
Zhou, Jieqin [1 ]
Yang, Kui [1 ,2 ]
Luo, Liang [3 ]
Wang, Pan [4 ]
Wang, Zhiwei [5 ]
Ma, Jinxing [1 ]
机构
[1] Guangdong Univ Technol, Sch Ecol Environm & Resources, Key Lab City Cluster Environm Safety & Green Dev, Minist Educ, Guangzhou 510006, Peoples R China
[2] Beijing Normal Univ, Adv Interdisciplinary Inst Environm & Ecol, Zhuhai 519087, Peoples R China
[3] Univ Sci & Technol China, Dept Environm Sci & Engn, CAS Key Lab Urban Pollutant Convers, Hefei 230026, Peoples R China
[4] Shanghai Municipal Engn Design Inst Grp Co Ltd, Shanghai 200092, Peoples R China
[5] Tongji Univ, State Key Lab Pollut Control & Resource Reuse, Shanghai Inst Pollut Control & Ecol Secur, Adv Membrane Technol Ctr,Sch Environm Sci & Engn, Shanghai 200092, Peoples R China
关键词
Ammonia recovery; Pulsed electric field; Stack design; Chemical-free; Gas permeable membrane; DESALINATION; NITROGEN;
D O I
10.1016/j.watres.2024.121129
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Recovering ammonia from waste streams (e.g., urine) is highly desirable to reduce natural gas-based NH3 production and nitrogen discharge into the water environment. Electrochemical membrane stripping is an attractive alternative because it can drive NH4+ transformation to NH3 via cathodic OH- production; however, the conventional configurations suffer from relatively low ammonia recovery (<80 %) and significant acid/material usage for ammonia adsorption. To this end, we develop a novel stack system that simply uses an oxygen evolution reaction to in-situ produce acid from water, enabling chemical-free ammonia recovery from synthetic urine. In batch mode, the percentage removal and recovery increased respectively from 74.5 % to 97.9 % and 81.8 % to 92.7 % when the electrode pairs increased from 2 to 4 in the stack system. To address the gas-sparging issue that deteriorated ammonia recovery in continuous operation, pulsed electric field (PEF) mode was applied, resulting in similar to 100 % recovery under optimized conditions. At an ammonia removal rate of 35.1 g-N m(-2) h(-1) and electrical energy consumption of 28.9 kWh kg-N-1, our chemical-free system in PEF mode has achieved significantly higher ammonia recovery (>90 %) from synthetic urine. The total cost to recover 1 kg of NH3-N from real human urine was $15.9 in the proposed system. Results of this study demonstrate that this novel approach holds great promise for high ammonia recovery from waste streams, opening a new pathway toward sustainable nitrogen management.
引用
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页数:11
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