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Performance evaluation and organic mass balance for treatment of high strength wastewater by anaerobic hybrid membrane bioreactor

机译:厌氧混合膜生物反应器处理高强度废水的性能评价和有机物平衡

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The performance and chemical oxygen demand (COD) mass balance of a lab-scale anaerobic hybrid membrane bioreactor (An-HMBR), treating high strength wastewater, at mesophilic temperature, was investigated. Long-term (275 days) operation was carried out at various hydraulic retention times (HRTs), namely, 3, 2, 1, and 0.5 days corresponding to organic loading rate (OLR) of 1.06, 1.6, 3.2, and 6.4 kg COD/m~3d, respectively. An-HMBR achieved, COD removal of 97-87% at HRT of 3-0.5 days, respectively. The study showed that polyurethane foam as attached growth media adsorbed mixed liquor suspended solids and thereby reduced the load on the membrane by 42%. During COD mass balance, an additional 4-5% of COD balance was achieved by consideration of COD conversion to biomass. The results suggest that unknown COD fraction varies between 33 and 37%, which was attributed to the loss of gaseous as well as oversaturation of dissolved methane. Consideration of oversaturation leads to a COD mass balance of over 95%.
机译:研究了实验室规模的厌氧混合膜生物反应器(An-HMBR)在中温温度下处理高强度废水的性能和化学需氧量(COD)质量平衡。在各种水力停留时间(HRT)分别进行3天,2天,1天和0.5天的长期操作(275天),对应于有机负荷率(OLR)为1.06、1.6、3.2和6.4千克COD / m〜3d。在HRT为3-0.5天时,An-HMBR的COD去除率分别为97-87%。研究表明,聚氨酯泡沫作为附着的生长介质吸附了混合液中的悬浮固体,从而使膜上的负荷降低了42%。在化学需氧量质量平衡过程中,考虑到将化学需氧量转化为生物质,可以实现化学需氧量平衡的4-5%。结果表明,未知的COD分数在33%到37%之间变化,这归因于气体的损失以及溶解甲烷的过饱和。考虑过饱和会导致COD质量平衡超过95%。

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