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Anaerobic submerged membrane bioreactor (AnSMBR) treating low-strength wastewater under psychrophilic temperature conditions

机译:厌氧潜水膜生物反应器(AnSMBR)在低温条件下处理低强度废水

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An anaerobic submerged membrane bioreactor (AnSMBR) treating low-strength wastewater was operated for 90 days under psychrophilic temperature conditions (20 C). Besides biogas sparging, additional shear was created by circulating sludge to control membrane fouling. The critical flux concept was used to evaluate the effectiveness of this configuration. Biogas sparging with a gas velocity (Ug ) of 62 m/h together with sludge circulation (94 m/h) led to a critical flux of 7 L/(m~2 h). Nevertheless, a further increase in the U_g only minimally enhanced the critical flux. A low fouling rate was observed under critical flux conditions. The cake layer represented the main fouling resistance after 85 days of operation. Distinctly different volatile fatty acid (VFA) concentrations in the reactor and in the permeate were always observed. This fact suggests that a biologically active part of the cake layer contributes to degrade a part of the daily organic load. Hence, chemical oxygen demand (COD) removal efficiencies of up to 94% were observed. Nevertheless, the biogas balance indicates that even considering the dissolved methane, the methane yield were always lower than the theoretical value, which indicates that the organic compounds were not completely degraded but physically retained by the membrane in the reactor.
机译:厌氧浸没式膜生物反应器(AnSMBR)处理低强度废水在低温(20°C)下运行90天。除沼气喷射外,通过循环污泥产生额外的剪切力以控制膜污染。临界通量概念用于评估该配置的有效性。沼气以62 m / h的气体速度(Ug)喷射,并伴随着污泥循环(94 m / h)产生7 L /(m〜2 h)的临界通量。然而,U_g的进一步增加仅最小程度地提高了临界通量。在临界通量条件下观察到低结垢率。在运行85天后,滤饼层代表了主要的耐污垢性。始终观察到反应器和渗透液中挥发性脂肪酸(VFA)的浓度明显不同。这一事实表明,滤饼层的生物活性部分有助于降低部分日常有机负荷。因此,观察到高达94%的化学需氧量(COD)去除效率。然而,沼气平衡表明,即使考虑溶解的甲烷,甲烷的收率始终低于理论值,这表明有机化合物并未完全降解,而是被膜物理保留在反应器中。

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