Dept. of Civil Engineering, National Institute of Technology, Kisarazu College, 2-11-1 Kiyomidaihigashi, Kisarazu, Chiba, 292-0041, Japan.
Dept. of Civil and Environmental Engineering, Tohoku University, 6-6-06 Aza-Aoba, Aramaki, Aoba-ku, Sendai, Miyagi, 980-8579, Japan.
Water Res. 2016 Oct 1;102:138-146. doi: 10.1016/j.watres.2016.06.035. Epub 2016 Jun 16.
A practical-scale down-flow hanging sponge (DHS) reactor using third-generation (G3) sponge carriers was applied for treatment of the effluent from an up-flow anaerobic sludge blanket (UASB) reactor treating municipal sewage. The process performance of the DHS reactor filled with G3 sponge carriers (DHS-G3) was evaluated by conducting an on-site experiment in India over one year. The performance of the DHS-G3 for removal of organic matter and ammonium-nitrogen at a relatively short hydraulic retention time (HRT) of only 0.66 h satisfied the Indian effluent quality standards except for fecal coliform. The removal rate constants for total biochemical oxygen demand (BOD) and fecal coliform determined based on the water quality profiles along the DHS-G3 almost reached equilibrium approximately four months after the start of operation, i.e., 2.45 h(-1) for BOD and 2.30 h(-1) for fecal coliform, respectively. The oxygen utilization activity of retained sludge was determined to assess the distribution of heterotrophic and autotrophic bacteria along the DHS-G3. Nitrification was promoted in the lower portion of the DHS-G3 reactor in the duration with low organic load, while it decreased when the organic load was increased, probably due to proliferation of heterotrophic bacteria.
采用第三代(G3)海绵载体的实用型下流式悬挂式海绵(DHS)反应器被应用于处理上流式厌氧污泥床(UASB)反应器处理城市污水的出水。通过在印度进行为期一年的现场实验,评估了填充 G3 海绵载体的 DHS 反应器(DHS-G3)的工艺性能。在水力停留时间(HRT)仅为 0.66 h 的情况下,DHS-G3 对有机物和铵态氮的去除性能满足印度废水质量标准,但粪大肠菌群除外。根据 DHS-G3 沿程水质特征确定的总生化需氧量(BOD)和粪大肠菌群的去除速率常数在运行约四个月后几乎达到平衡,分别为 2.45 h(-1) 和 2.30 h(-1)。通过测定保留污泥的耗氧活性来评估异养菌和自养菌在 DHS-G3 中的分布。在低有机负荷期间,DHS-G3 反应器的下部促进了硝化作用,而当有机负荷增加时,硝化作用减少,可能是由于异养菌的增殖。