期刊文献+

流化填料型A^2O工艺处理城市污水中试研究 被引量:1

Study on the A^2O Process with Fluidized Carriers in Municipal Wastewater Treatment
下载PDF
导出
摘要 目的研究厌氧-缺氧-好氧(A2O)工艺对城市污水的去除特性.为已建污水处理厂的提标改造工程提供便于实施的工艺.方法将A2O工艺与生物膜法结合,通过向反应器好氧池中投加聚氨酯流化填料强化脱氮除磷效率.结果经A2O工艺处理的系统出水COD质量浓度为33.1 mg/L,NH+4-N质量浓度为4.56 mg/L,TN质量浓度为14 mg/L,TP质量浓度为0.43mg/L,好氧区对于TN的去除最高可达系统TN去除率的14.2%,好氧区内TN的流失说明系统中出现了明显的同步硝化反硝化现象.城市污水出水水质达到《城镇污水处理厂综合排放标准》一级A标准.结论 A2O工艺对于水质水量的变化具有较强的抗冲击负荷能力,投加填料后,即使在进水水质波动很大的情况下,系统对于水中污染物仍能保持很高的去除率,出水水质稳定. The purpose of this paper is to investigate the treatment efficiency of A^2O process treating munici- pal wastewater. It was a facilitated process which could be used in renovation project of sewage plant. Traditional A^2O process was combined with biofilm. Fluidized carriers were added into the aerobic zone to enhance the efficiency of nitrogen and phosphorus removal. The average effluent COD was 33.1 mg/L, NH4^+ -N was 4.56 mg/L, TN was 14 mg/L, and TP was 0. 43 mg/L. TN removal rate in aerobic zone was up to 14.2% in the system. TN loss of aerobic zone showed the phenomenon of simultaneous nitrification and denitrification happened. The effluent water quality achieved "Urban sewage treatment plant discharge standard" level A standard. The process had a strong resistance to impact load of water quality and quantity. After dosing fluidized carriers, even in the case of large fluctuations of water quality conditions, system could keep high pollutant removal rates, the effluent water quality was stable.
出处 《沈阳建筑大学学报(自然科学版)》 CAS 北大核心 2014年第3期557-561,共5页 Journal of Shenyang Jianzhu University:Natural Science
基金 国家自然科学基金项目(51108277)
关键词 流化填料 A^2O工艺 城市污水 同步硝化反硝化 fluidized carriers A^2O process municipal wastewater simultaneous nitrification and denitrification
  • 相关文献

参考文献8

二级参考文献68

共引文献48

同被引文献15

  • 1王有为,周选阳.活性污泥-超滤膜联合工艺提高城市污水回用率的探讨[J].硅谷,2008,1(21):93-93. 被引量:1
  • 2Nghiem L D, Coleman P J. NF/RO filtration of the hydrophobic inorganic compound trielosan: Transport meehanisms and the influence of membrane fouling [J]. Seppurif Teehnol,2008, 62:711 -718.
  • 3Wang F L, Tarabara V V. Pore blocking mech- anisms during early stages of membrane fouling by colloids [J].Journal of Colloid and Interface Science.2008.328 ( 2 ) ,464 - 469.
  • 4邢锴.膜生物反应器-反渗透组合系统中的膜污染研究[D].天津:天津大学,2011.
  • 5Gleick p H. The world' s water 2006 - 2007 [ R]. Chicago: The Biennial Report on Fresh- water Re - sources ,2006.
  • 6Mohsen N M, Montazerib P, Modarressc H. Removal of Cu2 + and Ni2 + from wastewater with a chelating agent and reverse osmosis processes [ J ]. Desalination, 2007, 217 ( 5 ) : 276 - 281.
  • 7Cristian C, Rafael G, Refian A, et al. Removal of trivalent chromium contaminant from aque- ous media using FAU-type zeolite membranes[J].J. Membr. Sci. ,2008(312) :163 - 173.
  • 8Bodalo A. Viability study of different reverse osmosis membranes for application in the terti- ary treatment of wastes from the tanning indus- try [J].Desalination,2005 ( 180 ) : 277 - 284.
  • 9Kim J, Di G, Francis A, et al. Autopsy of high- pressure membranes to compare effectiveness of MF and UF pretreatment in water reclama- tion [ J ]. Water Research, 2008,42 ( 3 ) : 697 - 706.
  • 10Tabatabai S, Kennedy M D, Amy G L, et al. Optimizing inline coagulation to reduce chemi- cal consumption in MF/UF systems[J].De- salination and Water Treatment, 2009,6 ( 2 ) : 94 - 101.

引证文献1

二级引证文献3

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