期刊文献+

深圳市光明污水处理厂低碳高氮污水处理工艺设计 被引量:1

Treatment Process Design of Sewage with Low Carbon and High Nitrogen in Shenzhen Guangming Sewage Treatment Plant
原文传递
导出
摘要 深圳市光明污水处理厂位于深圳市宝安区,远期设计总规模为25×104 m3/d,近期规模为15×104 m3/d。其污水具有明显的低碳高氮的特征,尤其雨季进水的碳源更低,这在我国南方的城市污水处理中具有一定的普遍性。该污水厂采用强化脱氮改良A2/O工艺,尾水达到《城镇污水处理厂污染物排放标准(》GB 18918—2002)的一级A标准。详细介绍了该工程的工艺流程、应对低碳高氮雨季合流污水的处理措施、主要构筑物的设计参数及工艺特点。 The Guangming Sewage Treatment Plant is located in Baoan district in Shenzhen, of which the long-term scale is 25 ×104 m^3/d, and the short-term scale is 15× 104 m^3/d. The sewage is characterized by low carbon and high nitrogen, especially much lower carbon source during rainy season, as it is common in municipal wastewater treatment in southern China to some extent. The plant adopts the improved A^2/O process for enhanced nitrogen removal, and the treated effluent quality meets the first class A criteria specified in Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant (GB 18918 -2002). The process flow of the project, treatment measures for combined sewage with low carbon high nitrogen in rainy season, design parameters of main structures and the process features are introduced.
作者 彭弘
出处 《中国给水排水》 CAS CSCD 北大核心 2011年第24期36-40,共5页 China Water & Wastewater
关键词 强化脱氮改良A2/O工艺 低碳高氮 碳源 O/A理念 雨季合流污水 improved A^2/O process for enhanced nitrogen removal low carbon and high nitrogen carbon source O/A conception combined sewage in rainy season
  • 相关文献

参考文献1

二级参考文献10

  • 1[1]Henze M,Kristensen G H,Strube R.Rate-capacity characterisation of wastewater for nutrient removal processes[J].Water Sci Technol,1994,29(7):101-107.
  • 2[3]Clayton J A,Ekama G A,Wentzel M C.Denitrification kinetics in biological nitrogen and phosphorus removal activated sludge systems treating municipal wastewaters[J].Water Sci Technol,1991,23:1025-1035.
  • 3[4]Ekama G A,Doid P L,Marais G v R.Procedures for determining influent COD fractions and the maximum specific growth rate of heterotrophs in activated sludge system[J].Water Sci Technol,1986,18 (6):91-114.
  • 4[5]Cokg(o)r E Ubar,S(o)zen S,Orhon D,et al.Respirometric analysis of activated sludge behaviour-I assessment of the readily biodegradable substrate[J].Water Res,1998,32(2):461 -475.
  • 5[6]Isaacs S H,Henze M,Sψeberg H,et al.External carbon source addition as a means to control an activated sludge nutrient removal process[J].Water Res,1994,28 (3):511-520.
  • 6[7]Katarzyna Kujawa,Bram Klapwijk.A method to estimate denitrification potential for predenitrification systems using NUR batch test[J].Water Res,1999,33 (10):2291-2300.
  • 7[8]Henze M.The influence of raw wastewater biomass on activated sludge oxygen respiration rates and denitrification rates[J].Water Sci Technol,1989,21:603-607.
  • 8[9]Henze M.Capabilities of biological nitrogen removal process from wastewater[J].Water Sci Technol,1991,23:669-679.
  • 9[11]Orhon Derin,Ales Esra,S(o)zen Seval,et al.Characterization and COD fractionation of domestic wastewaters[J].Environmental Pollution,1997,95 (2):191-204.
  • 10[12]Yeom Ick Tae,Nah Yoo Mi,Ahn Kyu Hong.Treatment of household wastewater using an intermittently aerated membrane bioreactor[J].Desalination,1999,124:193-204.

共引文献7

同被引文献1

引证文献1

二级引证文献11

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