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短程硝化反硝化倒置A~2/O工艺脱氮效果研究
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摘要
本论文采用短程硝化反硝化倒置A~2/O工艺对生活污水脱氮效果进行研究,首先通过倒置A~2/O工艺与常规A~2/O工艺的对比实验,确定倒置A~2/O工艺在保证COD去除率的前提下脱氮的优越性。然后对生物脱氮的相关机理进行了探讨,并对影响系统脱氮效果的各种因素(诸如温度、溶解氧浓度、污泥回流比、C/N比、pH值等)以及主要的运行机理进行了较详细的分析研究,试验结果表明,实现短程硝化反硝化最佳条件是:温度18~25℃,溶解氧DO=2mg/L,pH值在6.5~7.5范围内。短程硝化反硝化倒置A~2/O工艺最佳工艺参数为:C/N为3.48,污泥回流比为200%。
The short-cut nitrification and denitrification in the inverted A~2/O process was used for the analysis on denitrogenation characteristic of the sewage in the paper.The experiments testify that inverted A~2/O process is superior of denitrogenation to traditional A~2/O process in the premise of ensuring removal of COD.The paper discuss mechanism of nitrogen removal and study the various kinds of influence factors(such as temperature, dissolved oxygen concentration, sludge reflux ratio,C/N,PH,etc.),and detailed study the main operation mechanism.Optimal operating parameters are achieved in the short-cut nitrification and denitrification was:T=18~25℃,DO=2mg/L,pH=6.5~7.5;and in the short-cut nitrification and denitrification in the inverted A~2/O process was: C/N=3.48,R=200%。
引文
[1]张波,高廷耀.倒置A2/O工艺的原理与特点研究[J].中国给水排水, 2000, 16(7): 11-15.
    [2]袁林江,彭党聪,王志盈.短程硝化—反硝化生物脱氮[J].中国给水排水, 2000, 16(2): 29-31.
    [3]张代钧,卢培利,严晨敏,等.活性污泥2号模型用于城市污水处理厂脱氮除磷改造的研究[J].环境科学学报, 2003, 23(3): 332-337.
    [4] Van Dongen.The Sharon-Anammox Process for Treatment of Ammonium Rich Wastewater[J].Water Science and Technology,2001,44(1):153-160.
    [5] Johwan Ahn,Tomotaka Daidou,Satoshi Tsuneda,et al.Selection and dominance mechanisms of denitrifying phosphate-accumulating organisms in biological phosphate removal process[J].Biotechnology Letters,2001,23:2005–2008.
    [6] Jetten M S M,Sliekers O,Kuypers M,et al.Anaerobic ammonium oxidation by and freshwater planctomycete bacteria[J].Appl Microbiol Biotechnol,2003,63:107-114.
    [7]方士,李筱焕.高氨氮味精废水的亚硝化/反亚硝化脱氮研究[]J.环境科学学报,2001,21(1):79~83
    [8] Satoshi Tsuneda, TakashiOhno, Koichi Soejima,et al.Simultaneous nitrogen and phosphorus removalusing denitrifying phosphate-accumulating organisms in a sequencing batch reactor[ J]. Biochem Eng J, 2006, 21(3): 191-196.
    [9]张杰. A2/O工艺的固有缺欠和对策研究[J].给水排水, 2003, 29(3): 22-25.
    [10]王少坡,彭永臻,王淑莹等.不同硝态氮组成下反硝化过程控制参数pH变化规律[J].高技术通讯,2005,15(8):91-95.
    [11]左剑恶等.一种新型生物脱氮工艺—SHARON-ANAMMOX组合工艺.给水排水,2001,27(10):22-27.
    [12]胡宝兰,郑平,冯孝善.新型生物脱氮技术的工艺研究[J].应用与环境生物学报,1999,5(Suppl):68-73.
    [13]郑平,冯孝善,Jetten M S M,等.厌氧氨氧化菌基质转化特性的研究[[J].浙江农业大学学报,1997,23(4):409-413.
    [14] Jetten M S M,Wagner M,Fuerst J,et al.Microbiology and application of the anaerobic ammonium oxidation process[J].Cur Opin Biotechnol,2001,12:283-288.
    [15]崔连成.生物膜内亚硝化-厌氧氨氧化最捷脱氮研究[D].天津理工大学,2006.
    [16]顾夏声.废水生物才处理数学模式[M].北京:清华大学出版社,1992.
    [17]徐伟峰,顾国维,陈银广.生物脱氮除磷AsMZD模拟及机理研究[m].博士论文,同济大学,2006.
    [18] Philips S,Wyffels S,Sprengers R,etal.Oxygen-limited autotrophic nitrification/ denitrificationby ammonia oxidisers enables upward motion towards more favourable conditions[J].Appl MicrobiolBiotechnol,2002,59:557-566.
    [19]张波,高廷耀.生物脱氮除磷工艺厌氧/缺氧环境倒置效应[J].中国给水排水, 1997,13(3):7 -10.
    [20]张波,高廷耀.倒置AAO工艺的原理与特点研究[J].中国给水排水,2006,16(3):11-15.
    [21]高廷耀,周增炎.无脱氮除磷功能废水处理厂的改造—简易改造城市污水厂的三种脱氮除磷新工艺[J].同济大学学报(自科版),2000,28(3):324-327.
    [22]金有祥,张万勤.改良型A2/O工艺综述[J].科技交流,2002,32(2):75-78.
    [23]万年红.A2/O工艺的改良与设计应用[J].中国给水排水,2003,19(8):81-83.
    [24] Dapena-Mora A,Campos J L,Mosquera-Corral A,et al.Stability of the ANAMMOX process in a gas-lift reactor and a SBR[J].Journal of Biotechn- ology,2004,110:159-170.
    [25]高大文,彭永臻,王淑莹,等.交替好氧/缺氧短程硝化反硝化生物脱氮Ι.方法实现与控制[J].环境科学学报,2004,24(5):762~769.
    [26] Picioreanu C,van Loosdrecht M C,Heijnen J J.Two-Dimensional Model of Biofilm Detachment Caused by Internal Stress from Liquid Flow[J].Biotechnology and Bioengineering,2001,72(2):206-218.
    [27]郑兴灿,李亚新编著.污水除磷脱氮技术[M].北京:中国建筑工业出版社,1998.
    [28]张小玲.生物膜内亚硝化过程及反硝化特性研究[D].西安建筑科技大学,2001.
    [29] Lee D U,Lee S,Choi D,et al.Effects of external carbon source and empty bed contact time on simultaneous heterotrophic and sulfur utilizing autotrophic denitrification[J].Process Biochemistry,2001,36:1215-1224.
    [30]国家环保总局.水和废水监测分析方法(第4版)[M].北京:中国环境科学出版社, 2002.
    [31]Jetten M S M.New pathways for ammonia conversion in soil and aquatic systems[J].Plant and Soil,2001,230:9-19.
    [32]马皆文,杨文谰等.营养物缺乏引发的丝状菌膨胀研究[J].工业安全与环保,2005,vol.31(11):4-6
    [33] Satoshi Tsuneda,Takashi Ohno,Koichi Soejima,et al.Simultaneous nitrogen and phosphorus removal using denitrifying phosphate-accumulating organisms in a sequencing batch reactor[J].Biochemical Engineering Journal,2006,27:191-196.
    [34] Russow R,Sich.I.The formation of the trace gases NO and N2O in soils by the coupled processes of nitrication and denitrication:results of kinetic15N tracer investigations[J].Chemosphere-GlobalChange Science,2000,2:359-366.
    [35] Ingo Schmidt,Olav Sliekers,Markus Schmid,et al.New concepts of microbial treatment processes for the nitrogen removal in wastewater[J].FEMS Microbiology Reviews,2003,27:481-492.
    [36]张小玲,王志盈,彭党聪,等.低溶解氧下活性污泥法的短程硝化研究[J].中国给水排水,2003,19(7):7~11
    [37] MulkerrinsD,DobsonA DW,Colleran E. Parameters affecting biological phosphate removal from wastewaters[J]. Environ Int, 2004, 30(2): 120-125.
    [38] Walworth James,Braddock Joan,Woolard Craig. Nutrient and temperature interactions in biore mediation of cryic soils.Cold Regions Science and Technology,2001,32(2-3):85-91.
    [39] Ruiz G, Jeison D, Chamy R. Nitrification with high nitrite accumulation for the treatment of wastewater with high ammonia concentration. Wat Res, 2003,37: 1371~1377.

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