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Pretreatment of silk-dyeing industrial wastewater by UASB reactor

机译:UASB反应器预处理印染工业废水

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The objective of this study was to investigate the performance of the upflow anaerobic sludge blanket (UASB) reactor as the pretreatment system for silk-dyeing wastewater. Two laboratory-scale UASB reactors, with working volume of 15.59 l, were used during May 1998 to June 1999. The actual wastewater was diluted to reduce ammonium ion toxicity on anaerobic bacteria. The experiments were conducted at the organic loading rates (OLRs) of 0.52, 1.01, 1.04, 1.54 and 2.56 kgCOD/(m(3).d), treating only wastewater generated from the acid-dye process of mixed-species raw silk. It took approximately 41/2 months to reach the steady-state conditions. It was found that the COD removal was in the ranges of 74.1-85.3%, except at OLR 2.56 kgCOD/(m(3).d) where efficiency significantly dropped to 55.2%. The apparent color removal was in the similar trend as COD. During the study periods, wastewater input had various color shades while the effluent generally looked pale yellowish. The methane generation rates ranged from 0.18-0.31 m(3)/kg COD removed, with methane composition 81.0-88.1% in biogas. The average granule size in the sludge bed had slowly increased to 0.73 mm in the last experiment. It can be concluded that the UASB reactor is suitable as a pretreatment system for silk-dyeing wastewater. An OLR of 1 kgCOD/(m3.d) and an influent concentration diluted to 2,600 mgCOD/I are suggested while COD and apparent color removal efficiency of 80% and 70%, respectively, can be expected.
机译:这项研究的目的是研究上流厌氧污泥层反应器(UASB)作为印染废水预处理系统的性能。 1998年5月至1999年6月,使用了两个实验室规模的UASB反应器,工作容积为15.59 l。对实际废水进行了稀释,以减少铵离子对厌氧细菌的毒性。实验以有机负荷率(OLR)为0.52、1.01、1.04、1.54和2.56 kgCOD /(m(3).d)进行,仅处理混合物种生丝的酸染过程中产生的废水。达到稳态需要大约41/2个月的时间。结果发现,除OLR为2.56 kgCOD /(m(3).d)以外,COD的去除率在74.1-85.3%范围内,效率显着下降至55.2%。表观颜色去除的趋势与COD相似。在研究期间,废水输入有各种颜色的阴影,而流出物通常看起来是淡黄色的。甲烷生成速率范围为0.18-0.31 m(3)/ kg去除的COD,沼气中甲烷成分为81.0-88.1%。在上一个实验中,污泥床中的平均颗粒尺寸已缓慢增加至0.73 mm。可以得出结论,UASB反应器适合作为印染废水的预处理系统。建议的OLR为1 kgCOD /(m3.d),进水浓度稀释至2600 mgCOD / I,而COD和表观脱色效率分别为80%和70%。

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