溶解氧对氧化沟同步硝化反硝化脱氮比率的影响

薛武丹, 彭党聪, 王攀, 董涛. 溶解氧对氧化沟同步硝化反硝化脱氮比率的影响[J]. 环境工程学报, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738
引用本文: 薛武丹, 彭党聪, 王攀, 董涛. 溶解氧对氧化沟同步硝化反硝化脱氮比率的影响[J]. 环境工程学报, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738
Xue Wudan, Peng Dangcong, Wang Pan, Dong Tao. Effect of dissolved oxygen on nitrogen removal efficiency of simultaneous nitrification and denitrification in oxidation ditch[J]. Chinese Journal of Environmental Engineering, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738
Citation: Xue Wudan, Peng Dangcong, Wang Pan, Dong Tao. Effect of dissolved oxygen on nitrogen removal efficiency of simultaneous nitrification and denitrification in oxidation ditch[J]. Chinese Journal of Environmental Engineering, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738

溶解氧对氧化沟同步硝化反硝化脱氮比率的影响

  • 基金项目:

    陕西省科技统筹创新重大项目(2011KTZB-03-03-03)

  • 中图分类号: X703

Effect of dissolved oxygen on nitrogen removal efficiency of simultaneous nitrification and denitrification in oxidation ditch

  • Fund Project:
  • 摘要: 微孔曝气变速氧化沟是一种新型的氧化沟。本研究通过批式实验,测定同步硝化反硝化(SND)溶解氧抑制系数KO,依此计算不同DO浓度下的SND比率,并与实际运行状况进行对比。结果表明:活性污泥的KO为0.7801 mg/L;当DO浓度分别为1.2、1.0和0.8 mg/L时,理论的SND比率分别为45.11%、47.57%和50.88%,而相同条件下氧化沟中实际SND比率分别为47.38%、52.75%和60.31%;同步硝化反硝化在微孔变速氧化沟中是一种重要的脱氮路径。
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  • [1] 马勇,王淑莹,曾薇,等.A/O生物脱氮工艺处理生活污水中试(一)短程硝化反硝化的研究.环境科学学报,2006,26(5):703-709 Ma Yong,Wang Shuying,Zeng Wei,et al.A/O pilot-scale nitrogen removal process treating domestic wastewaterⅠ.The study of short-cut nitrification and denitrification.Acta Scientiae Circumstantiae,2006,26(5):703-709(in Chinese)
    [2] Liu Yanchen,Shi Hanchang,Xia Lan,et al.Study of operational conditions of simultaneous nitrification and denitrification in a Carrousel oxidation ditch for domestic wastewater treatment.Bioresource Technology,2010,101(3):901-906
    [3] Hao Xiaodi,Doddema H.J.,van Groenestijn J.W.Conditions and mechanisms affecting simultaneous nitrification and denitrification in a Pasveer oxidation ditch.Bioresource Technology,1997,59(2-3):207-215
    [4] Rittmann B.E.,Langeland W.E.Simultaneous denitrification with nitrification in single-channel oxidation ditches.Journal of Water Pollution Control Federation,1985,57(4):300-308
    [5] Daigger G.T.,Adams C.D.,Steller H.K.Diffusion of oxygen through activated sludge flocs:Experimental measurement,modeling,and implications for simultaneous nitrification and denitrification.Water Environment Research,2007,79(4):375-387
    [6] Yoo H.,Ahn K.H.,Lee H.J.,et al.Nitrogen removal from synthetic wastewater by simultaneous nitrification and denitrification (SND) via nitrite in an intermittently-aerated reactor.Water Research,1999,33(1):145-154
    [7] 葛士建,彭永臻,张亮,等.改良UCT分段进水脱氮除磷工艺性能及物料平衡.化工学报,2010,61(4):1009-1017 Ge Shijian,Peng Yongzhen,Zhang Liang,et al.Performance and material balance of modified UCT step feed enhanced biological nitrogen and phosphate removal process.CIESC Journal,2010,61(4):1009-1017(in Chinese)
    [8] Henze M.,IWA Task Group for Mathematica.Activated Sludge Models ASM1,ASM2,AMS2d and ASM3.London,UK:IWA Scientific and Technical Report Series,2000
    [9] 国家环境保护总局.水质 五日生化需氧量(BOD5)的测定稀释与接种法.北京:中国质检出版社,2009
    [10] 王社平,王卿卿,惠灵灵,等.分段进水A/O脱氮工艺反硝化速率的测定.环境工程,2008,26(3):56-58 Wang Sheping,Wang Qingqing,Hui Lingling et al.The determination of denitrification rate of step-feed A/O nitrogen removal process.Environmental Engineering,2008,26(3):56-58(in Chinese)
    [11] Barnard J.L.Biological nutrient removal without the addition of chemicals.Water Research,1975,9(5-6):485-490
    [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] Münch E.V.,Lant P.,Keller J.Simultaneous nitrification and denitrification in bench-scale sequencing batch reactors.Water Research,1996,30(2):277-284
    [14] Manser R.,Gujer W.,Siegrist H.Consequences of mass transfer effects on the kinetics of nitrifiers.Water Research,2005,39(19):4633-4642
    [15] Sarioglu M.,Insel G.,Artan N.,et al.Modelling of long-term simultaneous nitrification and denitrification (SNDN) performance of a pilot scale membrane bioreactor.Water Science and Technology,2008,57(11):1825-1833
    [16] Sarioglu M.,Insel G.,Artan N.,et al.Model evaluation of simultaneous nitrification and denitrification in a membrane bioreactor operated without an anoxic reactor.Journal of Membrane Science,2009,337(1-2):17-27
    [17] 彭党聪,韩芸,王晓昌,等.基于反应动力学的生物脱氮氧化沟分区供氧设计优化.给水排水,2011,37(8):44-46 Peng Dangcong,Han Yun,Wang Xiaochang,et al.Optimization of oxygen distribution in oxidation ditch for nitrogen removal on the basis of reaction kinetics.Water & Wastewater Engineering,2011,37(8):44-46(in Chinese)
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  • 收稿日期:  2014-06-13
  • 刊出日期:  2015-07-02
薛武丹, 彭党聪, 王攀, 董涛. 溶解氧对氧化沟同步硝化反硝化脱氮比率的影响[J]. 环境工程学报, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738
引用本文: 薛武丹, 彭党聪, 王攀, 董涛. 溶解氧对氧化沟同步硝化反硝化脱氮比率的影响[J]. 环境工程学报, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738
Xue Wudan, Peng Dangcong, Wang Pan, Dong Tao. Effect of dissolved oxygen on nitrogen removal efficiency of simultaneous nitrification and denitrification in oxidation ditch[J]. Chinese Journal of Environmental Engineering, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738
Citation: Xue Wudan, Peng Dangcong, Wang Pan, Dong Tao. Effect of dissolved oxygen on nitrogen removal efficiency of simultaneous nitrification and denitrification in oxidation ditch[J]. Chinese Journal of Environmental Engineering, 2015, 9(7): 3305-3310. doi: 10.12030/j.cjee.20150738

溶解氧对氧化沟同步硝化反硝化脱氮比率的影响

  • 1. 西安建筑科技大学环境与市政工程学院, 西安 710055
基金项目:

陕西省科技统筹创新重大项目(2011KTZB-03-03-03)

摘要: 微孔曝气变速氧化沟是一种新型的氧化沟。本研究通过批式实验,测定同步硝化反硝化(SND)溶解氧抑制系数KO,依此计算不同DO浓度下的SND比率,并与实际运行状况进行对比。结果表明:活性污泥的KO为0.7801 mg/L;当DO浓度分别为1.2、1.0和0.8 mg/L时,理论的SND比率分别为45.11%、47.57%和50.88%,而相同条件下氧化沟中实际SND比率分别为47.38%、52.75%和60.31%;同步硝化反硝化在微孔变速氧化沟中是一种重要的脱氮路径。

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