Influencing factors of denitrification of glycans and transformation characteristics of internal carbon sources

被引:0
作者
Liu X. [1 ]
Guo H. [1 ]
Zhang S. [1 ]
Huang L. [1 ]
机构
[1] School of Environmental Science and Engineering, Dalian Jiaotong University, Dalian, 116028, Liaoning
来源
Huagong Xuebao/CIESC Journal | 2019年 / 70卷 / 03期
关键词
Absorption; Anaerobic; Denitrifying glycan; Internal carbon source denitrification; Polymers;
D O I
10.11949/j.issn.0438-1157.20181076
中图分类号
学科分类号
摘要
The denitrifying glycan bacteria were successfully enriched in the SBR reactor with sodium acetate as the carbon source and NO3--N as the electron acceptor, and the effects of the influent C/N ratio (3.3,6.7,10), electron acceptors (NO3--N, NO2--N), carbon source types (sodium acetate, glucose) on the activity of denitrifying glycans and the conversion characteristics of internal carbon sources were further investigated by batch experiment. The results show that the higher the influent C/N ratio, the higher the NOx--N removal rate of the system, and the more PHB synthesis in the anaerobic section, but the influent C/N ratio is too high, which leads to the predominance of common denitrifying bacteria. The denitrification efficiency of the internal carbon source is suitable for the influent C/N ratio of 6.7. The DGAOs system with NO3--N as the electron acceptor for long-term cultivation is not domesticated by NO2--N, and has good anti-NO2--N. Nitrification performance, after adding the same concentration of NO2--N as NO3--N, the system NOx--N removal rate is 89.6%; when glucose is used as the carbon source, the amount of PHB synthesized by DPAOs in the anaerobic section is only 79.5% of PHB with sodium acetate as the carbon source, and the anaerobic glucose utilization rate is only 72.8%, which is much smaller than the utilization rate of sodium acetate. © All Right Reserved.
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页码:1127 / 1134
页数:7
相关论文
共 33 条
[1]  
Ahn J.H., Kim S., Park H., Et al., N<sub>2</sub>O emissions from activated sludge processes, 2008-2009: results of a national monitoring survey in the United States, Environmental Science and Technology, 44, 12, pp. 4505-4511, (2010)
[2]  
Li Y.B., Wang S.Y., Yuan Q., Et al., Effect of NO<sub>x</sub><sup>-</sup>-N on anaerobic fermentation and denitrification performance of primary sludge, CIESC Journal, 64, 4, pp. 1431-1437, (2013)
[3]  
Chen Y.Z., Peng Y.Z., Wang J.H., Et al., A<sup>2</sup>/O biological aerated filter process denitrification phosphorus removal, CIESC Journal, 62, 3, pp. 797-804, (2011)
[4]  
Kuba T., van Loosdrecht M.C.M., Heijnen J.J., Phosphorus and nitrogen removal with minimal COD requirement by integration of denitrifying dephosphatation and nitrification in a two-sludge system, Water Research, 30, 7, pp. 1702-1710, (1996)
[5]  
Zhang W.T., Hou F., Liu Q.S., Et al., Effect of HRT and aeration on denitrifying phosphorus removal performance of AAO-BAF system, CIESC Journal, 65, 4, pp. 1436-1442, (2014)
[6]  
Wang M.X., Zhao W.H., Huang Y., Et al., Effect of nitration time distribution ratio of N-SBR unit on operating performance of A<sub>2</sub>N<sub>2</sub> system, CIESC Journal, 67, 12, pp. 5259-5267, (2016)
[7]  
Cech J.S., Hartman P., Competition between polyphosphate and polysaccharide accumulating bacterial in biological phosphorus removal systems, Wat. Res, 27, pp. 1219-1225, (1993)
[8]  
Matsuo Y., Effect of the anaerobic SPT on enhanced biological phosphorus removal, Water Sci. Tech., 30, 6, pp. 193-202, (1994)
[9]  
Satoh H., Mino T., Matsuo T., Deterioration of enhanced biological phosphorus removal by the domination of microorganisms without polyphosphate accumulation, Water Sci. Tech., 30, 6, pp. 203-211, (1994)
[10]  
Cech J.S., Hartman P., Glucose induced breakdown of enhanced biological phosphorus removal, Environ. Tech., 11, pp. 651-656, (1990)