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首页> 外文期刊>Waste Management >Anaerobic hybrid membrane bioreactor for treatment of synthetic leachate: Impact of organic loading rate and sludge fractions on membrane fouling
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Anaerobic hybrid membrane bioreactor for treatment of synthetic leachate: Impact of organic loading rate and sludge fractions on membrane fouling

机译:用于治疗合成渗滤液的厌氧杂化膜生物反应器:有机加载速率和污泥馏分对膜污垢的影响

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摘要

In the present study, the treatment of synthetic landfill leachate was carried out using a lab-scale anaerobic hybrid membrane bioreactor (An-HMBR). The reactor was operated for 250 days at two days of hydraulic retention time (HRT). Average chemical oxygen demand (COD) removal efficiency was ≥ 88% at steady-state conditions at 100% raw leachate. As organic loading rate (OLR) increased from 1.6 to 13.9 Kg COD m~(-3) d~(-1) flux gradually declined from 70 to 52 L/m~2 h (LMH) within 250 days. Chemical membrane cleaning enhanced the flux up to 75% of the initial flux at the final stage of the reactor. Reversible fouling (>90%) dominated over irreversible fouling (<8%). Membrane fouling was mainly caused by extracellular polymeric substances (EPS) fraction, which resulted in cake layer formation on the ceramic membrane used in the An-HMBR system. Membrane resistance increased with variables in the following order OLR > MLSS (mixed liquor suspended solids) > EPS > SMP (soluble microbial products). A nonlinear regression model developed for prediction of membrane resistance at different OLR can predict with an error of ±7%.
机译:在本研究中,使用Lab-ScaleAnaerobic杂交膜生物反应器(AN-HMBR)进行合成垃圾填埋渗滤液的处理。在液压保留时间(HRT)的两天内操作反应器250天。在100%原料渗滤液的稳态条件下,平均化学需氧量(COD)去除效率≥88%。由于有机加载速率(OLR)从1.6升至13.9kg COD m〜(-3)d〜(-1)通量在250天内逐渐下降70至52l / m〜2 h(lmh)。化学膜清洗在反应器的最终阶段的初始通量的磁共量增强了助焊剂。可逆污垢(> 90%)以不可逆转的污垢(<8%)为主。膜污垢主要由细胞外聚合物物质(EPS)级分引起,从而导致在AN-HMBR系统中使用的陶瓷膜上形成蛋糕层。膜抗性在下列顺序中的变量增加(混合液悬浮固体)> EPS> SMP(可溶性微生物产品)中的变量增加。用于预测不同OLR的膜抗性的非线性回归模型可以预测误差为±7%。

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