CO2-driven ion exchange for ammonium recovery from source-separated urine

被引:0
作者
Zhou, Lei [1 ]
Wang, Dian [1 ]
Yu, Jiayu [1 ]
Zhang, Hongyi [1 ]
Dong, Hang [1 ]
机构
[1] Tianjin Univ, Georgia Tech Shenzhen Inst GTSI, Shenzhen 518067, Peoples R China
关键词
Ion exchange regeneration; Ammonium recovery; Urine resource recovery; Circular economy; CO2; utilization; CARBON-DIOXIDE; WASTE-WATER; PARTIAL DEMINERALIZATION; NITROGEN RECOVERY; REMOVAL; CO2; PHOSPHATE;
D O I
10.1016/j.watres.2025.123132
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Nitrogen recovery from urine and CO2 utilization are both vital for achieving a circular economy and mitigating climate change. Divided engineering solutions have been proposed to address either problem, but there is still a lack of integrated technologies to simultaneously tackle the two tasks. We demonstrated CO2-driven ion exchange for nitrogen recovery (CIXNR) from urine and evaluated the process in Malawi. By comprehensively studying the ion exchange chemistry using a proton-form weak acid cation exchanger (WAC-H), we revealed the suppressed adsorption capacity caused by counterion releasing. Regulating aqueous pH optimized the WAC-H capacity, particularly, by the natural buffering capacity provided by bicarbonate in the hydrolyzed urine. CO2 regeneration achieved over 75 % nitrogen recovery in a multi-cycle test with synthetic hydrolyzed urine. A higher CO2 pressure resulted in faster regeneration kinetics due to a lower aqueous pH and higher proton concentration gradient. Our field outreach activity in Malawi indicated future research demand in adapting the system for resource-limited, rural, and no-electricity areas. We envision this study to inspire more integrated solutions to tackle both circular economy and climate actions and call for more field outreach activities to facilitate urine technology adoption in developing countries.
引用
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页数:10
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