Simulation study on the effect of dissolved oxygenon single-stage granular sludge autotrophic nitrogen removal system
LI Bo-lin, REN Xiao-ling, LI-Ye, WANG-Yue, WANG-Wei, LIANG Ya-nan
Hubei Key Laboratory of Mineral Resources Processing and Environment, School of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, China
The effect of dissolved oxygen (DO) on single-stage granular sludge autotrophic denitrification in a sequencing batch reactor system was evaluated through coupling of mass transfer process of granule sludge, vegetation processes of ammonia oxidizing bacteria (AOB), aerobic ammonia-oxidizing bacteria (AAOB), nitrite-oxidizing bacteria (NOB) and denitrifying bacteria, and endogenous respiration processes of aerobic and anoxic bacteria. A kinetic model of autotrophic denitrification granular sludge was developed based on activated sludge model 3 (ASM3) and the shortcut nitrification-nitrification-denitrification model, and subsequently the substrate concentration distribution within granular sludge was predicted. The results showed the ratio of aerobic zone to anoxic zone in granular sludge decreased from 3:1 to 0.4:1 when DO concentration decreased from 0.6mg/L to 0.4mg/L. Based on the matrix reaction rate equation, a system kinetic model of granular sludge single-stage autotrophic nitrogen removal was developed to predict system performance. The predicted result of total nitrogen removal rate (89%) was slightly lower than the actual measured removal rate (95%).
国际水协废水生物处理设计与运行数学模型课题组等.活性污泥数学模型[M]. 上海:同济大学出版社, 2002:22-25. IWA taskgroup on mathematical modelling for design and operation of biological wastewater treatment et al.Activated sludge models ASM1, ASM2, ASM2d and ASM3[M]. Shanghai:Tongji University Press, 2002:22-25.
[2]
Isaka K, Kimura Y, Yamamoto T, et al. Complete autotrophic denitrification in a single reactor using nitritation and anammox gel carriers[J]. Bioresource Technology, 2013,147:96-101.
[3]
孙培德,等.活性污泥动力学模型及数值模拟导论[M]. 北京:化学工业出版社, 2010:57-73. Sun P D, et al. Dynamic models and numerical simulations for activated sludge processes[M]. Beijing:Chemical Industry Press, 2010:57-73.
[4]
Gujer W, Henze M, Mino T, et al. Activated sludge model No.3[J]. Water Science and Technology, 1999,39(1):183-193.
[5]
Koch G, Kuhni M, Gujer W, et al. Calibration and validation of Activated Sludge Model No.3 for Swiss municipal wastewater[J]. Water Research. 2000,34(14):3580-3590.
[6]
Ni B J, Yu H Q. Simulation of heterotrophic storage and growth processes in activated sludge under aerobic conditions[J]. Chemical Engineering Journal. 2008,140(1-3):101-109.
[7]
Nowak O, Svardal K, Schweighofer P. The dynamic behaviour of nitrifying activated sludge system in?uenced by inhibiting wastewater compounds[J]. Water Science and Technology, 1995,31(2):115-124.
[8]
Iacopozzi I, Innocenti V, Marsililibelli S, et al. A modified activated sludge model No.3(ASM3) with two-step nitrification-denitrification[J]. Environmental Modelling & Software, 2007,22(6):847-861.
[9]
Zhou M, Gong J Y, Yang C Z, et al. Simulation of the performance of aerobic granular sludge SBR using modified ASM3model[J]. Bioresource Technology, 2013,127:473-481.
[10]
蔡庆.完全自养脱氮SBR反应器的运行、强化及模拟优化[D]. 重庆:重庆大学, 2013. Cai Q. Operation, enhancement and modeling optimization of completely autotrophic nitrogen removal over nitrite in SBR[D]. Chongqing:Chongqing University, 2013.
[11]
Pambrun V, Paul E, Sprandio M. Modeling the partial nitrification in sequencing batch reactor for biomass adapted to high ammonia concentrations[J]. Biotechnology Bioengineering, 2006,95(1):120-131.
[12]
Ni B J, Chen Y P, Liu S Y, et al. Modeling a granule-based anaerobic ammonium oxidizing (ANAMMOX) process[J]. Biotechnology and Bioengineering, 2009,103(3):490-499.
[13]
Lhenze M. Activated sludge models ASM1, ASM2, ASM2d and ASM3[M]. London:IWA Pub, 2000.
[14]
Moussa M S, Hooijmans C M, Lubberding H J, et al. Modelling nitrification, heterotrophic growth and predation in activated sludge[J]. Water Research, 2005,39(20):5080-5098.
[15]
Laspidou C S, Rittmann B E. Non-steady state modeling of extracellular polymeric substances, ksoluble microbial products, and active and inert biomass[J]. Water Research, 2002,36(8):1983-1992.
[16]
Rikmann E, Zekker I, Tominqas M, et al. Sulfate-reducing anammox for sulfate and nitrogen containing wastewaters[J]. Desalination and Water Treatment, 2016,57(7):3132-3141.
[17]
Hao X D, Heijnen J J, Van L, et al. Sensitivity analysis of a biofilm model describing a one-stage completely autotrophic nitrogen removal (CANON) process[J]. Biotechnology Bioengineering, 2002,77(3):266-277.
[18]
Beun J J, Heijnen J J, Van L, et al. N-removal in a granular sludge sequencing batch airlift reactor[J]. Biotechnology Bioengineering, 2001,75(1):82-92.
[19]
Chiu Z C, Chen M Y, Lee D J, et al. Diffusivity of oxygen in aerobic granules[J]. Biotechnology Bioengineering, 2006,94(3):505-513.
[20]
国家环境保护总局.水和废水监测分析方法[M]. 4版.北京:中国环境科学出版社, 2009:88-284. State Environmental Protection Administration. Water and wastewater monitoring and analysis methods (Fourth Edition)[M]. Beijing:China Environmental Science Press, 2009:88-284.
[21]
Mulkerrins D, Dobson A, Colleran E. Parameters affecting biological phosphate removal from wastewaters[J]. Environment International. 2004,30(2):249-259.
[22]
Yang Y F, Li Y, Gu Z L, et al. Quick start-up and stable operation of a one-stage deammonification reactor with a low quantity of AOB and ANAMMOX biomass[J]. Scienceofthe Total Environment, 2019,654:933-941.
[23]
窦元.DO浓度对全程自养脱氮颗粒污泥脱氮效能的影响研究[D]. 哈尔滨:哈尔滨工业大学, 2015. Dou Y. Study on the impact of DO concentration on the denitrification effect of completely autotrophic nitrogen removal granular sludge[D]. Harbin:Harbin Institute of Technology, 2015.
[24]
李亚峰,张晓宁,刘洪涛,等.DO的质量浓度和温度对配合厌氧氨氧化的亚硝化反应的影响[J]. 沈阳建筑大学学报(自然科学版). 2012,28(4):716-721. Li Y F, Zhang X N, Liu H T, et al. The impact of DO mass concentration and temperatureon ANAMMOX adopting[J]. Journal of Shenyang Jianzhu University Natural Science, 2012,28(4):716-721.
[25]
Huang X, Urata K, Wei Q, et al. Fast start-up of partial nitritation as pre-treatment for anammox in membrane bioreactor[J]. Biochemical Engineering Journal, 2016,105:371-378.
[26]
肖洋,廖德祥,李小明,等.全程自养脱氮颗粒污泥培养及动力学研究[J]. 环境科学, 2009,30(9):2667-2673. Xiao Y, Liao D X, Li X M, et al. Enrichment and dynamic analysis of deammonification granules[J]. Environmental Science, 2009,30(9):2667-2673.
[27]
Xu Z, Zeng G, Yang Z, et al. Biological treatment of landfill leachate with the integration of partial nitrification, anaerobic ammonium oxidation and heterotrophic denitrification[J]. Bioresource Technology, 2010,101(1):79-86.
[28]
李冬,崔少明,梁瑜海,等.溶解氧对序批式全程自养脱氮工艺运行的影响[J]. 中国环境科学, 2014,34(5):1131-1138. Li D, Cui S M, Liang Y H, et al. The effect of dissolved oxygen on running CANNON process in sequencing batch reactor[J]. China Environmental Science, 2014,34(5):1131-1138.
[29]
张姚,韩海成,王伟刚,等.溶解氧对CANON颗粒污泥自养脱氮性能的影响[J]. 中国环境科学, 2017,37(12):4501-4510. Zhang Y, Han H C, Wang W G, et al. Impact of dissolved oxygen on autotrophic nitrogen removals of the granular sludge in a CANNON process[J]. China Environmental Science, 2017,37(12):4501-4510.