期刊文献+

改良UCT分段进水深度脱氮除磷工艺反硝化动力学性能 被引量:4

The Denitrification Dynamics of Modified UCT Step Feed Enhanced Biological Nutrients Removal Process
下载PDF
导出
摘要 采用序批试验研究了在T=(15±1)℃条件下以生活污水、污泥水解酸化上清液、乙酸钠、甲醇、乙醇和葡萄糖为电子供体的活性污泥的反硝化性能以及pH变化规律和动力学特性.结果表明,乙酸钠的比反硝化速率和比耗碳速率最高,分别为4.13 mg/(g.h)和29.8 mg/(g.h),但其反硝化能力最低.污泥水解酸化上清液的反硝化速率与乙酸钠相当.反硝化菌需经若干周期的驯化后才能适应甲醇和乙醇电子供体.当要求直接提高反硝化速率时,不宜选择甲醇和乙醇为碳源.而葡萄糖电子供体系统在前10~120 min出现短暂的'ρ(NOx--N)还原停滞平台',当大分子葡萄糖糖酵解为小分子有机物后,反硝化过程才顺利进行,糖酵解过程是葡萄糖反硝化过程的限速步骤.此外,不同电子供体反硝化过程pH变化规律可以间接指示反硝化动力学特性,其缺氧异养菌产率系数为0.68~0.73. Batch experiments are conducted to investigate the denitrification prosperities,denitrification dynamics and pH variation with municipal wastewater,supernatants of sludge hydrolyzed acidification,acetic sodium,methanol,ethanol and glucose as electron donors as well as nitrate as electron acceptor under T=(15±1)℃.The results show that the maximum specific denitrification rate and specific organic compounds utilization rate,which is 4.13mg/h and 29.8mg/h,respectively,were attained when acetic sodium is used as the electron donor,whereas the lowest denitrification potential was also observed.As for supernatants of sludge hydrolyzed acidification,its denitrification performance is nearly as same as acetic sodium.Furthermore,denitrification bacteria can adapt to methanol and ethanol until a period of sludge acclimations,so these two electron donors could not be used as soon as it needed to improve the denitrification efficiency.As for glucose,there is a "ρ(NO-x-N) reduction stop platform" during 10-120mins of reaction process,after glucose molecules decomposing into small molecules organisms the denitrification could go on successfully,so glycoside is the rate-limiting step of denitrification with glucose as the electron donor.Besides,pH indicates the denitrification characteristics of different electron donors with heterotrophy anoxic yields of 0.68-0.73.
出处 《北京工业大学学报》 EI CAS CSCD 北大核心 2011年第3期433-439,共7页 Journal of Beijing University of Technology
基金 国家'十一五'重大科技专项课题(2008ZX07317-007-105) 北京工业大学第八届研究生科技基金项目(ykj-2010-3738) 2008年中韩环境共同技术研究项目
关键词 分段进水 反硝化动力学 碳源 电子供体 比反硝化速率 step feed denitrification dynamics carbon source electron donors specific denitrification rate
  • 相关文献

参考文献23

  • 1PAI T Y, TSAI Y P, CHOU Y J, et al. Microbial kinetic analysis of three different types of EBNR process [ J]. Chemosphere, 2004, 55( 1 ) : 109-118.
  • 2ZHU G B, PENG Y Z, ZHAI L M, et al. Performance and optimization of biological nitrogen removal process enhanced by anoxic/oxic step feeding[ J]. Biochemical Engineering Journal, 2009, 43 (3) : 280-287.
  • 3ZHU G B, PENG Y Z, MA B, et al. Optimization of anoxic/oxic step feeding active sludge process with fuzzy control model for improving nitrogen removal [ J ]. Chemical Engineering Journal, 2009, 151 ( 1/3 ) : 195-201.
  • 4BARLINDHAUG J, ODEGARD H. Thermal hydrolysate as a carbon source for denitrification [ J ]. Water Science and Technology, 1996, 33(12): 99-108.
  • 5ZAYED G, WINTER J. Removal of organic pollutants and nitrate from wastewater from the dairy industry by denitrification [ J]. Applied Microbiology and Biotechno!ogy, 1998, 49(4) : 469-474.
  • 6HENZE M, GRADY C J, GUJER W, et al. Activated sludge model No. 1. IAWPRC scientific and Technical Report No. 1 [M]. London: IAWPRC, 1987.
  • 7HENZE M, GUJER W, MINO T, et al. Activated sludge model No. 2. IAWQ scientific and Technical Report No. 3 [ M]. London: IAWPRC, 1987.
  • 8SAGE M, DAUFIN G, GI~SAN-GUIZIOU G, et al. Denitrification potential and rates of complex carbon source from dairy effluents in activated sludge system [ J]. Water Research, 2006, 40(14) : 2747-2755.
  • 9KUJAWA K, KLAPWIJK B. A method to estimate denitrification potential for pre-denitrifieation systems using NUR batch tests [J]. Water Research, 1999, 33(10): 2291-2300.
  • 10NYBERG U, ASPEGREN H, ANDERSSON B, et al. Full-scale applications of nitrogen removal with methanol as carbon source[J]. Water Science and Technology, 1992, 26(5/6) : 1077-1086.

同被引文献75

  • 1池勇志,李毓,吴丽萍.城市污水前置反硝化生物脱氮工艺的动力学计算[J].天津城市建设学院学报,2004,10(2):122-124. 被引量:4
  • 2PENG Yong-zhen,MA Yong,WANG Shu-ying.Denitrification potential enhancement by addition of external carbon sources in a pre-denitrification process[J].Journal of Environmental Sciences,2007,19(3):284-289. 被引量:37
  • 3J. C. Akunna,C. Bizeau,R. Moletta.Denitrification in anaerobic digesters: Possibilities and influence of wastewater COD/N-NOX ratio[J].Environmental Technology.1992(9)
  • 4Natuscka M. Lee,Thomas Welander.The effect of different carbon sources on respiratory denitrification in biological wastewater treatment[J].Journal of Fermentation and Bioengineering.1992(3)
  • 5deBarbadillo C,Miller P,Ledwell S.A comparison of operating issues and dosing requirements for alternative carbon sources in denitrification filters[].Proceedings of the Water Environment FederationWEFTEC.2008
  • 6Michael R. Betlach,James M. Tiedje.Kinetic Explanation for Accumulation of Nitrite, Nitric Oxide, and Nitrous Oxide During Bacterial Denitrification[].Applied and Environmental Microbiology.1981
  • 7Carrera, J.,Vicent, T.,Lafuente, F.J.Influence of temperature on denitrification of an industrial high-strength nitrogen wastewater in a two-sludge system[].Water SA.2003
  • 8Ciggin, A.S.,Karahan, O.,Orhon, D.Effect of biochemical storage on the denitrification potential of acetate in sequencing batch reactors[].Water Science and Technology;Waste Management Problems in Agro-Industires.2007
  • 9Christensson, M.,Lie, E.,Welander, T.A comparison between ethanol and methanol as carbon sources for denitrification[].Water Science and Technology;Nutrient Removal.1994
  • 10Cho, E.S.,Ahn, K.-H.,Molof, A.H.Comparison of sequentially combined carbon with sole carbon in detrification and biological phosphorus removal[].Water Science and Technology.2004

引证文献4

二级引证文献52

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部