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处理低浓度复杂废水的分段式和非分段式上流式厌氧污泥床(USSB 和 UASB)反应器的性能。

Performance of staged and non-staged up-flow anaerobic sludge bed (USSB and UASB) reactors treating low strength complex wastewater.

机构信息

El Colegio de la Frontera Sur, Carretera Antiguo Aeropuerto Tapachula, Chiapas, Mexico.

出版信息

Biodegradation. 2010 Sep;21(5):737-51. doi: 10.1007/s10532-010-9339-y. Epub 2010 Feb 22.

Abstract

The use of anaerobic processes to treat low-strength wastewater has been increasing in recent years due to their favourable performance-costs balance. For optimal results, it is necessary to identify reactor configurations that are best suited for this kind of application. This paper reports on the comparative study carried out with two high-rate anaerobic reactor systems with the objective of evaluating their performances when used for the treatment of low-strength, complex wastewater. One of the systems is the commonly used up-flow anaerobic sludge blanket (UASB) reactor. The other is the up-flow staged sludge bed (USSB) system in which the reactor was divided longitudinally into 3, 5 and 7 compartments by the use of baffles. The reactors (9 l) were fed with a synthetic, soluble and colloidal waste (chemical oxygen demand (COD) < 1000 mg/l) and operated at 28 degrees C and 24 h hydraulic retention time. Intermediate flow hydraulics, between plug-flow and completely-mixed, in the UASB and 7 stages USSB reactors allowed efficient degradation of substrates with minimum effluent concentrations. Low number of compartments in the USSB reactors increased the levels of short-circuiting thus reducing substrate removal efficiencies. All reactors showed high COD removal efficiencies (93-98%) and thus can be regarded as suitable for the treatment of low strength, complex wastewater. Staged anaerobic reactors can be a good alternative for this kind of application provided they are fitted with a large enough (> or =7) number of compartments to fully take advantage of their strengths. Scale factors seem to have influenced importantly on the comparison between one and multi staged sludge-bed reactors and, therefore, observations made here could change at larger reactor volumes.

摘要

近年来,由于厌氧工艺具有良好的性能成本比,因此越来越多地用于处理低浓度废水。为了获得最佳效果,有必要确定最适合这种应用的反应器配置。本文报告了对两种高负荷厌氧反应器系统进行的对比研究,目的是评估它们在处理低浓度、复杂废水时的性能。其中一个系统是常用的上流式厌氧污泥床(UASB)反应器。另一个是上流式分段污泥床(USSB)系统,该系统通过使用挡板将反应器纵向分为 3、5 和 7 个隔室。这些反应器(9 升)采用合成的、可溶的和胶体的废水(化学需氧量(COD)<1000 毫克/升)进行进料,在 28°C 和 24 小时水力停留时间下运行。UASB 和 7 段 USSB 反应器中存在介于推流式和完全混合式之间的中间流动水力学,允许有效降解基质,同时将出水中的浓度降至最低。USSB 反应器中的隔室数量较少会增加短路的程度,从而降低基质去除效率。所有反应器都表现出高的 COD 去除效率(93-98%),因此可被视为适用于处理低浓度、复杂废水。分段厌氧反应器可以作为这种应用的一种很好的选择,只要它们配备了足够大(≥7)数量的隔室,以充分利用其优势。规模因素似乎对单段和多段污泥床反应器之间的比较有重要影响,因此,这里的观察结果可能会在更大的反应器体积下发生变化。

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