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

机译:UASB直接处理生活污水的潜在弊端的技术评估

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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.
机译:评估了由上流厌氧污泥层(UASB)反应器组成的生活污水处理系统的性能和稳定性。在莱索托等发展中国家,对使用这种系统直接处理此类含有大量悬浮固体(SS)的废水进行了技术评估。随着时间的流逝,就颗粒物的积累及其总体质量而言,污泥床的演变受到了严密的监控。废水的平均总化学需氧量(COD t )为522 mgL -1 ,该系统可去除80%的有机物。反应器系统中的污泥产生量很高(高达70%的流入化学需氧量(COD)为悬浮固体),平均每100天需要从反应器中重复排放污泥。考虑到厌氧反应器中产甲烷菌的微妙平衡,污泥提取后会引起微生物菌群的扰动,并加剧了反应器的不平衡。这进一步导致反应器性能下降,并因此导致在处理生活污水时UASB工艺的总体可持续性下降。此外,该系统无法去除大量营养素氮和磷。需要额外的处理步骤以去除悬浮的固体和营养物,从而有效地处理这种废水。

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