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Influence of relaxation modes on membrane fouling in submerged membrane bioreactor for domestic wastewater treatment

机译:弛豫模式对埋藏膜生物反应器膜污染的影响

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摘要

Relaxation and backwashing have become an integral part of membrane bioreactor (MBR) operations for fouling control. This study was carried out on real municipal wastewater to evaluate the influence of different operational strategies on membrane fouling at equivalent water yield. Four relaxation modes (MBR10+0, MBR10+1, MBR10+1.5 and MBR10+2) were tested to analyze membrane fouling behavior. For the optimization of relaxation modes, fouling rate in terms of trans-membrane pressure, hydraulic resistances and characteristics of fouling fractions were analyzed. It has been observed that cake layer resistance was minimum in MBR10+1.5 but pore blockage resistance was increased in all relaxation modes. Moreover, high instantaneous flux contributed significantly to fouling rate at the initial stage of MBR operations. Relaxation modes were also efficient in removing irreversible fouling to some extent. Under all relaxation modes, COD removal efficiency ranged from 92 to 96.5%. Ammonium and TP removal were on the lower side due to the short solids and hydraulic retention time.
机译:放松和反冲洗已成为膜生物反应器(MBR)操作的一部分,用于污垢控制。该研究进行了真正的市政废水,评估不同运营策略对等同水产量膜污染的影响。测试四种弛豫模式(MBR10 + 0,MBR10 + 1,MBR10 + 1.5和MBR10 + 2)以分析膜污垢行为。为了优化弛豫模式,分析了跨膜压力,液压电阻和结垢级分的污垢率的污垢率。已经观察到,在MBR10 + 1.5中,滤饼层电阻最小,但所有松弛模式都增加了孔隙障碍。此外,高瞬时通量在MBR操作初始阶段的初始阶段进行了显着贡献。放松方式也有效地在一定程度上去除不可逆转的污垢。在所有放松模式下,COD去除效率范围为92至96.5%。由于固体和液压保留时间短,铵和TP除去在下侧。

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