富集联合体泵处理法对河流中溶解态S2−的去除效果增强

Chen Song, Yajun Shi, Hongjie Gao, H. Ren, Xiaoling Liu
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引用次数: 0

摘要

S2−是重污染河流中常见的污染物之一。在本研究中,采用泵-处理富集联合体法(PEPEC)去除S2−。建立了S2−去除的动力学模型,并根据动力学模型的结果分析了PEPEC的入流比。结果表明,PEPEC作业中,当进水比控制在2%时,S2−去除率可达97.5% ~ 0.5%。同时,通过模拟离地试验和现场试验,对其去除效果和运行性能进行了评价。与原位工艺相比,在120 h的生物处理过程中,PEPEC表现出稳定的运行性能,出水中S2−、COD、NH3-N和TP的浓度分别约为0.5、20、0.5和0.5 mg/L。PEPEC工艺的时间(8 h /批)和联合体投加量(3 g /批)明显低于原位工艺。PEPEC对重污染河流的生物处理具有潜在的优势。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Enhanced removal of dissolved S2− from a river by the pump-and-treat ex-situ process with enriched consortium
S2− is one of the common pollutants in heavily polluted rivers. A pump-and-treat ex-situ process with enriched consortium (PEPEC) was used to remove S2− in this study. The kinetic model of S2− removal was developed, and the inflow ratio of the PEPEC was analyzed according to the results of the kinetic models. The results showed that the S2− removal ratio could reach 97.5% 5 0.5%, when the inflow ratio was controlled at 2% for the PEPEC operation. Meanwhile, the removal efficiency and operation performance were assessed for both the simulating ex-situ and in-situ bench-scale tests. Compared with the in-situ processes, the PEPEC showed a stable operation performance during 120 h of bio-treatment, and the concentrations of S2−, COD, NH3-N and TP in the effluent reached approximately 0.5, 20, 0.5 and 0.5 mg/L, respectively. The time consumption (8 h for one batch) and consortium dosage (3 g for the whole operation) in the PEPEC were significantly less than those in the in-situ processes. The PEPEC presented some potential advantages for the bio-treatment of a heavily polluted river.
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