期刊文献+

两点进水在倒置AAO流程除磷中的作用 被引量:3

Influence of two-point-fed on P removing from inverse AAO process
下载PDF
导出
摘要 利用计算机仿真研究两点进水对倒置AAO流程除磷的作用,发现将污水按选择池进水流量与厌氧池进水流量的分配比(简称进水流量分配比)为1.0/0、0.9/0.1、0.8/0.2、0.7/0.3、0.6/0.4、0.5/0.5分流到选择池和厌氧池,会影响中等COD负荷(200~220 mg/L)下该流程的除磷效果。原因在于,污水分流到厌氧池虽然能提高厌氧池内乙酸浓度,但同时会因稀释作用而降低厌氧池及好氧池中聚磷菌的浓度,影响聚磷菌厌氧释磷及好氧吸磷的作用。两点进水对低COD负荷(140~180 mg/L)及高COD负荷(260~340 mg/L)下该流程的除磷效果无明显影响,前者因各反应池(除二沉池外)内聚磷菌浓度本身很低,后者则因各反应池内聚磷菌浓度本身很高,改变进水流量分配比不会改变这2种情况下各反应池内聚磷菌释磷或吸磷的强度。 An inverse AAO process in a newly built wastewater treatment plant was computer simulated to study the function of two-point-fed mode for P removing.The wastewater was fed into AAO process from two points of selecting tank(Q1) and anaerobic tank(Q2) with different flow ratio(Q1/Q2).Applied the inverse AAO process for treating middle COD load(200-220 mg/L) wastewater,reducing the flow ratio will lower its P removing function.The reason was that although the carbon source to the anaerobic tank was increased by inputting more raw wastewater to the anaerobic tank,the concentration of polymeric phosphorus organisms(PAO) in the anaerobic and the aerobic tanks was reduced,and as a result,the function of anaerobic P released and aerobic P absorbance was weakened.Applied the inverse AAO process for treating low COD load(140-180 mg/L) wastewater and high COD load(260-340 mg/L) wastewater,flow ratio of two-point-fed mode had no significant influence on P removing because changing the flow ratio could not cause any essential effect on the PAO concentration in the two cases.
出处 《环境污染与防治》 CAS CSCD 北大核心 2010年第12期43-47,71,共6页 Environmental Pollution & Control
基金 上海市科委基金资助项目(No.072312003)
关键词 两点进水 倒置 AAO 流程 除磷效果 进水流量 厌氧池 聚磷菌 COD负荷 流量分配比 反应池 菌浓度 选择池 内聚 乙酸浓度 厌氧释磷 稀释作用 好氧吸磷 分流 仿真研究 inverse AAO process two-point-fed acetic acid phosphate phosphate-accumulating organisms simulation
  • 相关文献

参考文献5

二级参考文献21

  • 1张杰,臧景红,杨宏,刘俊良.A^2/O工艺的固有缺欠和对策研究[J].给水排水,2003,29(3):22-26. 被引量:139
  • 2董姗燕,姚重华.单级活性污泥过程数学模型ASM2D参数的灵敏度分析[J].环境化学,2005,24(2):129-133. 被引量:17
  • 3郝晓地,朱景义,曹秀芹.污水强化除磷工艺的现状与未来[J].中国给水排水,2005,21(11):37-40. 被引量:9
  • 4Brun R, Kuhni M, Siegrist H, et al. 2002. Practical identifiability of ASM2D parameters systematic selection and tuning of parameter subsets[ J]. Water Research, 36(19) : 4113-4127.
  • 5Copp J B, Spanjers H, Vanrolleghem P A, 2002. Respirometry in Control of the Activated Sludge Process: Benchmarking Control Strategies [ R ]. IWA Scientific and Technical Reports No. 11. London : IWA Publishing, 13- 15.
  • 6Gernaey K V, Van Loosdrecht M C M, Henze M, et al. 2004. Activated sludge wastewater treatment plant modeling and simulation : State of the art [J]. Environmental Modeling & Software, 19:763-783.
  • 7Henze M, Gujer W, Mino T. 1995. Activated Sludge Model No. 2[R]. IWA Scientific and Technical Report No. 3. London: IWA Publishing, 3-8.
  • 8Henze M, Gujer W, Mino T, et al, 1999. Activated Sludge Model No. 2d, ASM2D [ J ]. Water Science and Technology, 39 ( 1 ) : 165-182.
  • 9Hao X D, Van Loosdrecht M C M, Meijer S C F. 2001. Model-based evaluation of two BNR processes: UCT and A (2)N [ J]. Water Research, 35(12) : 2851-2860.
  • 10Meijer S C F, Van Loosdrecht M C M, Heijnen J J. 2001. Metabolic modeling of full-scale biological nitrogen and phosphorus removing WWTP's[J]. Water Research,35 (11): 2711-2723.

共引文献28

同被引文献40

引证文献3

二级引证文献16

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