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Enhanced bioremoval of refractory compounds from dyeing wastewater using optimized sequential anaerobic/aerobic process

机译:使用优化的顺序厌氧/好氧工艺增强了印染废水中难熔化合物的生物去除

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The upflow anaerobic sludge blanket process followed by the biological aerated filter process was employed to improve the removal of color and recalcitrant compounds from real dyeing wastewater. The highest removal efficiency for color was observed in the anaerobic process, at 8-h hydraulic retention time, seeded with the sludge granule. In the subsequent aerobic process packed with the microbe-immobilized polyethylene glycol media, the removal efficiency for chemical oxygen demand increased significantly to 75 %, regardless of the empty bed contact time. The average influent non-biodegradable soluble chemical oxygen demand was 517 mg/L, and the average concentration in effluent from the anaerobic reactor was 363 mg/L, suggesting the removal of some recalcitrant matters together with the degradable ones. The average nonbiodegradable soluble chemical oxygen demand in effluent from the aerobic reactor was 87, 93, and 118 mg/L, with the removal efficiency of 76, 74, and 67 %, at 24-, 12-, and 8-h empty bed contact time, respectively. The combined anaerobic sludge blanket and aerobic cell-entrapped process was effective to remove the refractory compounds from real dyeing wastewater as well as in reducing organic loading to meet the effluent discharge limits. This integrated process is considered an effective and economical treatment technology for dyeing wastewater.
机译:采用上流式厌氧污泥覆盖工艺,然后进行生物曝气滤池工艺,以改善从实际印染废水中去除颜色和难降解化合物的能力。在厌氧过程中,在8小时的水力停留时间下,污泥颗粒播种时观察到最高的颜色去除效率。在随后的装有微生物固定化聚乙二醇介质的需氧工艺中,无论空床接触时间如何,化学需氧量的去除效率均显着提高至75%。进水不可生物降解的平均可溶性化学需氧量为517 mg / L,厌氧反应器的出水平均浓度为363 mg / L,表明去除了一些难降解物质和可降解物质。好氧反应器出水的平均不可生物降解的可溶性化学需氧量分别为87、93和118 mg / L,在24、12和8小时空床下的去除效率分别为76、74和67%接触时间。厌氧污泥覆盖层和好氧细胞包裹工艺相结合,可有效去除实际印染废水中的难处理化合物,并降低有机负荷,以达到废水排放极限。该综合过程被认为是用于染色废水的有效且经济的处理技术。

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