Polymer-flooding produced water treatment using an electro-hybrid ozonation-coagulation system with novel cathode membranes targeting alternating filtration and in situ self-cleaning
•A novel CM-E-HOC was firstly put forward to apply in produced water treatment.•The CM-E-HOC showed higher removal efficiency than the CM-EC processes.•Both reversible and irreversible membrane fouling were mitigated in the CM-E-HOC.•Alternating filtration in the CM-E-HOC can realize higher water pr...
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Veröffentlicht in: | Water research (Oxford) 2023-04, Vol.233, p.119749-119749, Article 119749 |
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Sprache: | eng |
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Zusammenfassung: | •A novel CM-E-HOC was firstly put forward to apply in produced water treatment.•The CM-E-HOC showed higher removal efficiency than the CM-EC processes.•Both reversible and irreversible membrane fouling were mitigated in the CM-E-HOC.•Alternating filtration in the CM-E-HOC can realize higher water production rate.•Excellent flux recovery can be achieved in the CM-E-HOC via in situ self-cleaning.
Polymer-flooding produced water is more difficult to treat for reinjection compared with normal produced water because of the presence of residual hydrolyzed polyacrylamide (HPAM). A novel cathode membrane integrated electro-hybrid ozonation-coagulation (CM-E-HOC) process was proposed for the treatment of polymer-flooding produced water. This process achieved in situ self-cleaning by generated microbubbles in the cathode membrane. The CM-E-HOC process achieved a higher suspended solid (SS), turbidity and PAM removal efficiency than the CM-EC process. The SS in the CM-E-HOC effluent was ≤ 20 mg/L SS, which met the reinjection requirements of Longdong, Changqing Oilfield, China (Q/SYCQ 08,011–2019) at different current densities (3, 5 and 10 mA/cm2). The CM-E-HOC process greatly mitigated both reversible and irreversible membrane fouling. Therefore, excellent flux recovery was obtained at different in situ self-cleaning intervals during the CM-E-HOC process. Furthermore, alternating filtration achieved continuous water production during the CM-E-HOC process. On one hand, the effective removal of aromatic protein-like substances and an increase in oxygen-containing functional groups were achieved due to the enhanced oxidation ability of the CM-E-HOC process, which decreased membrane fouling. On the other hand, the CM-E-HOC process showed improved coagulation performance because of the increased oxygen-containing functional groups and polymeric Fe species. Therefore, larger flocs with higher fractal dimensions were generated, and a looser and more porous cake layer was formed on the membrane surface during the CM-E-HOC process. Consequently, the CM-E-HOC process exhibited better in situ self-cleaning performance and lower filtration resistance than the CM-EC process.
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ISSN: | 0043-1354 1879-2448 |
DOI: | 10.1016/j.watres.2023.119749 |