Pre-ozonation coupled with forward osmosis with fertilizer as draw solution for simultaneous wastewater treatment and agricultural irrigation

被引:0
|
作者
Yang, Fu [1 ,2 ]
Wang, Xingbao [3 ]
Shan, Yuanyuan [4 ]
Wu, Chongde [1 ,2 ]
Zhou, Rongqing [1 ,2 ]
Hengl, Nicolas [5 ]
Pignon, Frederic [5 ]
Jin, Yao [1 ,2 ]
机构
[1] Sichuan Univ, Coll Biomass Sci & Engn, Chengdu 610065, Peoples R China
[2] Sichuan Univ, Educ Minist, Key Lab Leather & Engn, Chengdu 610065, Peoples R China
[3] Taiyuan Univ Technol, State Key Lab Clean & Efficient Coal Utilizat, Taiyuan 030024, Peoples R China
[4] Taiyuan Univ Technol, Inst New Carbon Mat, Coll Mat Sci & Engn, Taiyuan 030024, Peoples R China
[5] Univ Grenoble Alpes, Grenoble INP, LRP, CNRS,Inst Engn Univ Grenoble Alpes, F-38000 Grenoble, France
关键词
Tannery wastewater; Ozone; Membrane fouling; Forward osmosis; Fertilizer; GAS PRODUCED WATER; LEATHER INDUSTRY; ULTRAFILTRATION; PRETREATMENT; MEMBRANES; MITIGATION; RECOVERY; REMOVAL; NANOFILTRATION; DESALINATION;
D O I
10.1016/j.desal.2024.118187
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Membrane-based processes have emerged as effective solutions for treating tannery wastewater. Persistent membrane fouling remains a significant obstacle to long-term operational sustainability, and residual pollutants often persist in the treated effluent. To address these challenges, we investigated an integrated ozone-forward osmosis (O3 3-FO) process, with a focus on evaluating the efficacy of pre-ozonation in alleviating membrane fouling, as well as exploring the possibilities of this integrated process for the reuse of tannery wastewater. Fertilizer, specifically 2 M Ca(NO3)2, 3 ) 2 , served as the draw solution (DS) in this process. The findings reveal that the integrated system demonstrated remarkable pollutant retention capabilities. Notably, no metal was detected in the fertilizer. Therefore, the integrated process not only dilutes the fertilizer but also minimizes the risk of heavy metal contamination to both crops and soil. Furthermore, pre-ozonation effectively mitigated membrane fouling, resulting in an increase in membrane flux with a maximum increase of 20.98 % at 0.6 L/min. Orthogonal partial least squares-discriminant analysis (OPLS-DA) revealed pre-ozonation has the most significant impact on four parameters: water flux (Jw), J w ), chemical oxygen demand (COD), fouling resistance (Rf) R f ) and oxidation reduction potential (ORP). Meanwhile, ammonium nitrogen (NH4-N) 4-N) variation, dissolved organic carbon (DOC) variation and ORP played an important role in the four systems. Multi-criteria decision analysis (MCDA) showed that the 0.2 L/min O3 3-FO system achieved the highest score (0.66), followed by 0.6 L/min (0.53), 0.4 L/min (0.41) and 0 L/min (0.29). This research offers a theoretical framework for the synergistic integration of advanced oxidation and membrane technology in the treatment of industrial wastewater.
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页数:12
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