Sodium hypochlorite-assisted osmotic backwashing for mitigating forward osmosis membrane fouling during pre-concentrating wastewater

Hai Duc Minh Tran, Hideaki Sano, Sandrine Boivin, Naoki Ohkuma, Mitsuharu Terashima, Takahiro Fujioka
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Abstract

Forward osmosis (FO) membrane has drawn substantial attention to pre-concentrating organic matter in wastewater for biogas production. However, membrane fouling control is an ongoing challenge for the feasibility of the FO system. Although chemical cleaning using a caustic solution (e.g., solution pH = 11) can remove organic foulants on the polyamide-based membranes, it can damage cellulose triacetate (CTA)-based FO membrane due to hydrolysis. This study assessed the efficacy of sodium hypochlorite (NaClO)-assisted osmotic backwashing to mitigate CTA-based FO membrane fouling during pre-concentrating primary wastewater effluent. The cleaning strategy employing a low concentration of NaClO showed a restoration of water flux higher than conventional hydraulic flushing and sole osmotic backwashing. The water flux after NaClO-assisted osmotic backwashing (NaClO concentrations = 10–80 mg/L) reached 97–102%. Irreversible foulants on the membrane surface were fully removed by NaClO concentration from 20 to 80 mg/L. During four filtration cycles using a 40 mg-NaClO/L cleaning solution, the reverse salt flux increased from 4.3 to 6.3 g/m2h. This indicates that for a long-term operation, applying lower concentrations of NaClO (e.g., 20 mg/L) may be needed to avoid the changes in reverse salt flux. This study suggests that FO membranes during pre-concentrating primary wastewater effluent can be stably operated with NaClO-assisted osmotic backwashing.
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次氯酸钠辅助渗透反冲洗减轻预浓缩废水中正向渗透膜污染
正渗透(FO)膜在预浓缩废水中的有机物以生产沼气方面引起了广泛的关注。然而,膜污染控制一直是FO系统可行性面临的挑战。虽然使用苛性碱溶液(例如溶液pH = 11)进行化学清洗可以去除聚酰胺基膜上的有机污染物,但由于水解会损坏三醋酸纤维素(CTA)基FO膜。本研究评估了次氯酸钠(NaClO)辅助渗透反冲洗在一次污水预浓缩过程中减轻cta基FO膜污染的效果。采用低浓度NaClO的清洗策略恢复的水通量高于常规液压冲洗和单渗透反冲洗。NaClO辅助渗透反冲洗(NaClO浓度= 10 ~ 80 mg/L)后的水通量达到97 ~ 102%。当NaClO浓度为20 ~ 80 mg/L时,膜表面的不可逆杂质被完全去除。在使用40 mg-NaClO/L清洗液的4次过滤循环中,反盐通量从4.3 g/m2h增加到6.3 g/m2h。这表明,对于长期操作,可能需要使用较低浓度的NaClO(例如20 mg/L)来避免反向盐通量的变化。本研究表明,在naclo辅助渗透反冲洗的条件下,初级废水预浓缩出水中FO膜可以稳定运行。
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