内置缺氧区的改良型Pasveer氧化沟工艺脱氮除磷性能研究

徐立, 杨殿海, 刘巍, 沈昌明. 内置缺氧区的改良型Pasveer氧化沟工艺脱氮除磷性能研究[J]. 环境工程学报, 2013, 7(3): 908-912.
引用本文: 徐立, 杨殿海, 刘巍, 沈昌明. 内置缺氧区的改良型Pasveer氧化沟工艺脱氮除磷性能研究[J]. 环境工程学报, 2013, 7(3): 908-912.
Xu Li, Yang Dianhai, Liu Wei, Shen Changming. Research on improving biological nutrient removal by a modified Pasveer oxidation ditch with additional internal anoxic zones[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 908-912.
Citation: Xu Li, Yang Dianhai, Liu Wei, Shen Changming. Research on improving biological nutrient removal by a modified Pasveer oxidation ditch with additional internal anoxic zones[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 908-912.

内置缺氧区的改良型Pasveer氧化沟工艺脱氮除磷性能研究

  • 基金项目:

    国家"水体污染控制与治理"科技重大专项(2008ZX07316)

  • 中图分类号: X703

Research on improving biological nutrient removal by a modified Pasveer oxidation ditch with additional internal anoxic zones

  • Fund Project:
  • 摘要: 针对传统Pasveer氧化沟内缺氧段碳源难以被反硝化菌充分利用的问题,采用内置缺氧区的改良型Pasveer氧化沟工艺,并进行中试规模实验研究,考察了不同内回流比条件下系统的脱氮除磷效果。研究结果表明,在内回流比为200%的情况下,系统的脱氮除磷效果最好,出水TN和TP的浓度分别降至12.7 mg/L和0.34 mg/L,去除率分别达到61.9%和89.2%。内置缺氧区的设置一方面能使有限的碳源充分用于反硝化,另一方面,促使了反硝化吸磷现象的发生,这使得系统在进水碳源较低的情况下仍能够获得上佳的脱氮除磷效果。但是,过高的内回流比会导致好氧区亚硝酸盐的积累,这对生物除磷是不利的。
  • [1] 建设部. 全国污水处理厂数据统计, 2006
    [2] Hao X. D., Doddema H. J., Groenestijn J. W. V. Conditions and mechanisms affecting simultaneous nitrification and denitrification in a Pasveer oxidation ditch. Bioresour. Technol., 1997, 59(2-3): 207-215
    [3] 汤兵, 王五洲, 石太宏. 低碳源条件下反硝化同步除磷脱氮的研究. 工业水处理, 2007, 27(12):49-51 Tang Bin, Wang Wuzhou, Shi Taihong. Simultaneous removal of phosphorus and nitrogen with denitrifying technique in low carbon source. Industrial Water Treatment, 2007, 27(12):49-51 (in Chinese)
    [4] Mulkerrins D., Dobson A. D. W., Colleran E. Parameters affecting biological phosphate removal from wastewaters. Environ. Int., 2004, 30(2): 249-259
    [5] Plósz B. G. Optimization of the activated sludge anoxic reactor configuration as a means to control nutrient removal kinetically. Water Res., 2007, 41(8): 1763-1773
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    [7] Wang Y. Y., Peng Y. Z., Stephenson T. Effect of influent nutrient ratios and hydraulic retention time (HRT) on simultaneous phosphorus and nitrogen removal in a two-sludge sequencing batch reactor process. Bioresour. Technol., 2009, 100(14): 3506-3512
    [8] Ma J., Peng Y. Z., Wang S. Y., et al. Denitrifying phosphorus removal in a step-feed CAST with alternating anoxic-oxic operational strategy. J. Environ. Sci-China, 2009, 21(9): 1169-1174
    [9] Peng Y. Z., Wang X. L., Wu W. M., et al. Optimisation of anaerobic/anoxic/oxic process to improve performance and reduce operating costs. J. Chem. Technol. Biotechnol., 2006, 81(8): 1391-1397
    [10] Kuba T., Murnleitner E., van Loosdrecht M. C. M., et al. A metabolic model for biological phosphorus removal by denitrifying organisms. Biotechnol. Bioeng., 1996, 52 (6): 685-695
    [11] 彭轶, 彭永臻, 吴昌永. A2/O工艺中的反硝化除磷. 环境工程学报, 2008, 2(6):752-756 Peng Yi, Peng Yongzhen, Wu Changyong. Denitrifying phosphorus removal in A2/O process. Chinese Journal of Environmental Engineering, 2008, 2(6):752-756 (in Chinese)
    [12] 国家环境保护总局. 水和废水监测分析方法(第4版). 北京:中国环境科学出版社, 2002
    [13] Lesage N., Spèrandio M., Lafforgue C., et al. Calibration and application of a 1-D model for oxidation ditches. Chem. Eng. Res. and Des., 2003, 81(9): 1259-1264
    [14] Garrido J. M., van Benthum W. A. J., van Loosdrecht M. C. M., et al. Influence of dissolved oxygen concentration on nitrite accumulation in a biofilm airlift suspension reactor. Biotechnol. Bioeng., 1998, 53(2): 168-178
    [15] Zhao H., Mavinic D. S., Oldham W. K., et al. Controlling factor simultaneous nitrification and denitrification in a two-stage intermittent aeration process treating domestic sewage. Water Res., 1999, 33(4): 961-970
    [16] Saito T., Brdjanovic D., van Loosdrecht M. C. M. Effect of nitrite on phosphate uptake by phosphate accumulating organisms. Water Res., 2004, 38(17): 3760-3768
    [17] Zeng W., Li L., Yang Y. Y., et al. Denitrifying phosphorus removal and impact of nitrite accumulation on phosphorus removal in a continuous anaerobic-anoxic-aerobic (A2O) process treating domestic wastewater. Enzyme Microb. Technol., 2011, 48(2):134-142
    [18] Brdjanovic D., Slamet A., van Loosdrecht M. C. M., et al. Impact of excessive aeration on biological phosphorus removal from wastewater. Water Res., 1998, 32(1): 200-208
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  • 收稿日期:  2011-10-13
  • 刊出日期:  2013-03-18
徐立, 杨殿海, 刘巍, 沈昌明. 内置缺氧区的改良型Pasveer氧化沟工艺脱氮除磷性能研究[J]. 环境工程学报, 2013, 7(3): 908-912.
引用本文: 徐立, 杨殿海, 刘巍, 沈昌明. 内置缺氧区的改良型Pasveer氧化沟工艺脱氮除磷性能研究[J]. 环境工程学报, 2013, 7(3): 908-912.
Xu Li, Yang Dianhai, Liu Wei, Shen Changming. Research on improving biological nutrient removal by a modified Pasveer oxidation ditch with additional internal anoxic zones[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 908-912.
Citation: Xu Li, Yang Dianhai, Liu Wei, Shen Changming. Research on improving biological nutrient removal by a modified Pasveer oxidation ditch with additional internal anoxic zones[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 908-912.

内置缺氧区的改良型Pasveer氧化沟工艺脱氮除磷性能研究

  • 1. 同济大学污染控制与资源化研究国家重点实验室,上海 200092
基金项目:

国家"水体污染控制与治理"科技重大专项(2008ZX07316)

摘要: 针对传统Pasveer氧化沟内缺氧段碳源难以被反硝化菌充分利用的问题,采用内置缺氧区的改良型Pasveer氧化沟工艺,并进行中试规模实验研究,考察了不同内回流比条件下系统的脱氮除磷效果。研究结果表明,在内回流比为200%的情况下,系统的脱氮除磷效果最好,出水TN和TP的浓度分别降至12.7 mg/L和0.34 mg/L,去除率分别达到61.9%和89.2%。内置缺氧区的设置一方面能使有限的碳源充分用于反硝化,另一方面,促使了反硝化吸磷现象的发生,这使得系统在进水碳源较低的情况下仍能够获得上佳的脱氮除磷效果。但是,过高的内回流比会导致好氧区亚硝酸盐的积累,这对生物除磷是不利的。

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