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Anaerobic treatment of vinasses by a sequentially mixed moving bed biofilm reactor

机译:顺序混合移动床生物膜反应器厌氧处理酒糟

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Wine distillery wastewater, commonly called vinasses, was treated by an anaerobic moving bed biofilm reactor (AMBBR) with 32.9 litre available volume. The reactor was filled with 66% cylindrical polyethylene supports with density 0.84 g cm-3 as a biofilm carrier. The reactor was sequentially mixed by a submerged centrifugal pump fixed to the bottom, and each mixing time just lasted 1.25 minutes. The organic loading rate (OLR) of the reactor were increased from 1.6 to 29.6 g sCOD l~(-1) d~(-1) (soluble chemical oxygen demands -sCOD) and hydraulic retention time (HRT) was decreased from 6.33 to 1.55 days accordingly. Soluble COD removal efficiency was 81.3–89.2% at an OLR of 29.6 g sCOD l~(-1)d~(-1). At the end of the experiment, 83.4% total biomass was attached on support and the specific density of support in the reactor was 0.93–1.05 g cm-3, which increased by about 10.7–25% compared with that at the beginning of the study.
机译:酿酒厂废水(通常称为酒糟)是通过厌氧移动床生物膜反应器(AMBBR)处理的,该反应器的可用容积为32.9升。反应器填充有密度为0.84 g cm-3的66%圆柱形聚乙烯载体作为生物膜载体。通过固定在底部的浸入式离心泵依次混合反应器,并且每次混合时间仅持续1.25分钟。反应器的有机负载率(OLR)从1.6 g sCOD l〜(-1)d〜(-1)(可溶性化学需氧量-sCOD)增加到29.6 g,水力停留时间(HRT)从6.33减少到相应地为1.55天。在29.6 g sCOD l〜(-1)d〜(-1)的OLR下,可溶性COD去除效率为81.3–89.2%。在实验结束时,总生物量附着在载体上的比例为83.4%,反应器中载体的比重为0.93-1.05 g cm-3,比研究开始时增加了约10.7-25%。 。

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