Technical evaluation of potential drawbacks in direct UASB treatment of raw domestic sewage

S. Aiyuk, Philip Odonkor, N. Theko, A. V. van Haandel, W. Verstraete
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引用次数: 4

Abstract

The performance and stability of a domestic sewage treatment system consisting of an upflow anaerobic sludge blanket (UASB) reactor were assessed. This was to come up with a technical evaluation of using such a system to treat directly such wastewater containing high amounts of suspended solids (SS), in developing countries like Lesotho. Through time, the evolution of the sludge bed was monitored closely, in terms of accumulation of particulate matter and its general quality. The average total chemical oxygen demand (CODt) of the wastewater was 522 mgL−1, and the system could remove 80 % of the organic matter. The sludge production in the reactor system was high (up to 70 % of influent chemical oxygen demand (COD) found as suspended solid), necessitating repeated sludge discharges from the reactor, on average every 100 days. Considering the delicate balance of the methanogens in anaerobic reactors, perturbations of the microbiota arose following the sludge extractions, and these promoted reactor imbalance. This further brought about a decrease in reactor performance and hence of the general sustainability of the UASB process when treating domestic sewage. In addition, the system could not remove the macronutrients nitrogen and phosphorus. Additional treatment steps would be necessary to remove the suspended solids and nutrients, and thus to effectively treat such a wastewater.
直接UASB处理原生活污水潜在缺点的技术评价
对由上流式厌氧污泥毯(UASB)反应器组成的生活污水处理系统的性能和稳定性进行了评价。这是为了对在莱索托等发展中国家使用这种系统直接处理含有大量悬浮固体(SS)的废水进行技术评估。随着时间的推移,对污泥床的演变进行了密切监测,包括颗粒物的积累及其总体质量。废水的平均总化学需氧量(CODt)为522 mgL−1,系统可去除80%的有机物。反应器系统中的污泥产量很高(高达70%的进水化学需氧量(COD)为悬浮固体),需要从反应器中重复排放污泥,平均每100天排放一次。考虑到厌氧反应器中产甲烷菌的微妙平衡,污泥提取后微生物群出现了扰动,这些扰动促进了反应器的不平衡。这进一步导致反应器性能下降,因此在处理生活污水时UASB工艺的总体可持续性下降。此外,该系统不能去除大量营养元素氮和磷。额外的处理步骤将需要去除悬浮固体和营养物质,从而有效地处理这种废水。
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