Ma Hang, Zhu Qiang, Zhu Liang, Li Xiang, Huang Yong, Wei Fan-Kai, Yang Peng-Bing
School of Environment Science and Engineering, Suzhou University of Science and Technology, Suzhou 215002, China.
Institute of Environmental Biotechnology, Suzhou University of Science and Technology, Suzhou 215002, China.
Huan Jing Ke Xue. 2016 Jun 8;37(6):2235-2242. doi: 10.13227/j.hjkx.2016.06.029.
The effect of element sulfur particle size and type of the reactor on sulfur autotrophic denitrification reactor start-up was researched at room temperature(19-24℃) by using sulfur autotrophic denitrification bio-membrane reactor and anaerobic sludge bed biofilm reactor and inoculating anaerobic sludge. The research indicated that after 65 d operation, the bio-membrane reactor gained steady denitrification efficiency. With an influent NO-N of 150 mg·L, and an HRT of 3.3 h, the removal efficiencies of NO-N and TN were 91% and 77%, and the removal rate of TN was 0.67-0.83 kg·(m·d). The increase of volumetric loading rate of NO-N and production of nitrogen gas led to the floating of sludge in the anaerobic sludge bed biofilm reactor. With an influent NO-N of 185 mg·L and an HRT of 3.3 h, the maximum removal rate of NO-N of 1.1 kg·(m·d) was attained in anaerobic sludge bed biofilm reactor. But the increase of effluent NO-N and NO-N lowered the quality of effluent water seriously, and the floating of sludge affected the steady operation of the anaerobic sludge bed biofilm reactor. Sulfur particles with particle size of 0.8 mm and 3.0 mm were used as electron donors for start-up of two batch reactors. The experiment results indicated that the reactor which used sulfur particle size of 0.8 mm attained higher removal efficiency of NO-N and TN, and its effluent accumulated less NO-N compared with the reactor which used particle size of 3.0 mm.
在室温(19 - 24℃)下,采用硫自养反硝化生物膜反应器和厌氧污泥床生物膜反应器,接种厌氧污泥,研究了元素硫粒径和反应器类型对硫自养反硝化反应器启动的影响。研究表明,运行65 d后,生物膜反应器获得了稳定的反硝化效率。进水NO-N为150 mg·L,水力停留时间(HRT)为3.3 h时,NO-N和TN的去除率分别为91%和77%,TN去除速率为0.67 - 0.83 kg·(m³·d)。NO-N容积负荷率的增加和氮气的产生导致厌氧污泥床生物膜反应器中污泥上浮。进水NO-N为185 mg·L,HRT为3.3 h时,厌氧污泥床生物膜反应器中NO-N的最大去除速率达到1.1 kg·(m³·d)。但出水NO-N和NO₂-N的增加严重降低了出水水质,污泥上浮影响了厌氧污泥床生物膜反应器的稳定运行。采用粒径为0.8 mm和3.0 mm的硫颗粒作为两个批次反应器启动的电子供体。实验结果表明,与使用粒径为3.0 mm硫颗粒的反应器相比,使用粒径为0.8 mm硫颗粒的反应器对NO-N和TN的去除效率更高,且其出水积累的NO₂-N更少。