Optimization of the integrated nitrogen removal process of high ammonia nitrogen wastewater in BAF by adjusting the gas water ratio
LI Hai-xin, LIU Xiu-hong, YANG Zhong-qi, LIU Run-yu, WU Wen-jun, YANG Qing
National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Techndogy, Beijing University and Technology, Beijing 100124, China
In order to achieve efficient removal of nitrogen from high ammonia nitrogen wastewater at room temperature, this study selected three gas water ratio conditions, 8:1、12:1 and 15:1 respectively. It investigated the stable operation performance of partial nitrification-ANAMMOX integrated autotrophic nitrogen removal process of biological aerated filter (BAF) at room temperature. The results showed that gas water ratio (GWR) at the optimal operation time was 15:1under the condition of inlet ammonia nitrogen (NH4+-N) concentration of 400mg/L and reflux ratio of 1:1, ammonia nitrogen removal rate (ARE) was over 90%,total nitrogen (TN) removal load was 1.1kgN/(m3·d), and TN removal rate could reach 83%. When the GWR is 15:1,the DO is controlled around 2.41mg/L and 4.22mg/L, the amount of NH4+-N converted into nitrite (NO2--N) in water increased, and the ANAMMOX activity is enhanced. The real-time fluorescence quantitative PCR (QPCR) analysis of functional strains on the biofilm showed that when the GWR was 15:1, both ANAMMOX and AOB had the highest abundance, more than 1012 copies/g dry sludge. Therefore, integrated nitrogen removal has the best effect. At the same time, studies have shown that the ANAMMOX reaction is strengthened after increasing the gas water ratio and N2O is not generated in the ANAMMOX process. When the GWR is 15:1, the total release amount of N2O is the smallest, and the release factor is 0.0012.
李海鑫, 刘秀红, 杨忠启, 刘润雨, 武文君, 杨庆. 调整气水比优化高氨氮废水BAF一体化脱氮[J]. 中国环境科学, 2019, 39(9): 3807-3813.
LI Hai-xin, LIU Xiu-hong, YANG Zhong-qi, LIU Run-yu, WU Wen-jun, YANG Qing. Optimization of the integrated nitrogen removal process of high ammonia nitrogen wastewater in BAF by adjusting the gas water ratio. CHINA ENVIRONMENTAL SCIENCECE, 2019, 39(9): 3807-3813.
Guerrero L, Montalvo S, Huiliñir C, et al. Simultaneous nitrification-denitrification of wastewater:effect of zeolite as a support in sequential batch reactor with step-feed strategy[J]. International Journal of Environmental Science and Technology, 2016,13(10):2325-2338.
[2]
李亚峰,马晨曦,张驰.UASBB厌氧氨氧化反应器处理污泥脱水液的影响因素研究[J]. 环境科学, 2014,35(8):3044-3051. Li Y F, Ma C X, Zhang C. Influencing Factors of Sludge Liquor Treatment in UASBB[J]. Environmental Science, 2014,35(8):3044-3051.
[3]
孙洪伟,彭永臻,时晓宁,等.UASB-A/O工艺处理垃圾渗滤液短程生物脱氮的实现[J]. 中国环境科学, 2009,29(10):1059-1064. Sun H W, Peng Y Z, Shi X Y, et al. Achieving nitrogen removal from landfill leachate via UASB-A/O process[J]. China Environmental Science, 2009,29(10):1059-1064.
[4]
赵晴,梁俊宇,吕慧,等.AO-MBR工艺短程硝化反硝化处理垃圾渗滤液中试研究[J]. 北京工业大学学报, 2018,44(1):45-49. Zhao Q, Liang J Y, Lv H, et al. Pilot-scale Study on nitritation-Denitritation of Landfill Leachate by an AO-MBR Process[J]. Journal of Beijing University of Technology, 2018,44(1):45-49.
[5]
张亮,王淑莹,张树军,等.高氨氮污泥脱水液短程硝化反硝化的启动及稳定[J]. 环境工程学报, 2012,6(4):1064-1068. Zhang L, Wang S Y, Zhang S J, et al. Start up and maintenance of partial nitrification-denitrification of high strength ammonia sludge dewatering water[J]. Chinese Journal of Environmental Engineering, 2012,6(4):1064-1068.
[6]
王成,孟佳,李玖龄,等.升流式微氧生物膜反应器处理高氨氮低C/N比养猪废水的效能[J]. 化工学报, 2016,67(9):3895-3901. Wang C, Meng J, Li J L, et al. Pollutant removal efficiency in upflow microaerobic biofilm reactor treating manure-free piggery wastewater with low COD/TN ratio and high NH4+-N[J]. CIESC Journal, 2016,67(9):3895-3901.
[7]
俞彬,陈广升,王玉慧,等.A/O+BAF工艺处理高氨氮煤化工废水[J]. 中国给水排水, 2013,29(6):81-83+88. Yu B, Chen G S, Wang Y H, et al. A/O+BAF Process for Treatment of Coal Chemical Wastewater with High Ammonia Nitrogen[J]. CHINA WATER & WASTEWATER, 2013,29(6):81-83+88.
[8]
吴鹏,张诗颖,宋吟玲,等.ABR工艺ANAMMOX耦合短程硝化协同脱氮处理城市污水[J]. 环境科学, 2016,37(8):3108-3113. WU P, ZHANG S Y, SONG Y L, et al. Nitrogen Removal of Municipal Wastewater by ANAMMOX Coupled Shortcut Nitrification in Anaerobic Baffled Reactor[J]. Environmental Science, 2016, 37(8):3108-3113.
[9]
Lackner S, Gilbert E M, Vlaeminck S E, et al. Full-scale partial nitritation/Anammox experiences-An application survey[J]. Water Research, 2014,55:292-303.
[10]
Gao D, Lu J, Liang H. Simultaneous energy recovery and autotrophic nitrogen removal from sewage at moderately low temperatures[J]. Applied Microbiology and Biotechnology, 2014,98(6):2637-2645.
[11]
Wen X, Zhou J, Wang J, et al. Effects of dissolved oxygen on microbial community of single-stage autotrophic nitrogen removal system treating simulating mature landfill leachate[J]. Bioresource Technology, 2016,218:962-968.
[12]
Vo T T, Nguyen T P. Nitrogen removal from old landfill leachate with SNAP technology using biofix as a biomass carrier[J]. Journal of Bioscience and Bioengineering, 2016,122(2):188-195.
[13]
Daverey A, Su S, Huang Y, et al. Partial nitrification and Anammox process:A method for high strength optoelectronic industrial wastewater treatment[J]. Water Research, 2013,47(9):2929-2937.
[14]
Liu X, Wang H, Long F, et al. Optimizing and real-time control of biofilm formation, growth and renewal in denitrifying biofilter[J]. Bioresource Technology, 2016,209:326-332.
[15]
杨庆,谷鹏超,刘秀红,等.两种典型滤料厌氧氨氧化效果与工艺运行优化[J]. 化工学报, 2015,66(1):455-463. Yang Q, Gu P C, Liu X H, et al. Comparison of performance and optimizing process for two typical filter medias of ANAMMOX biofilters[J]. CIESC Journal, 2015,66(1):455-463.
[16]
杨庆,周桐,刘秀红,等.常温下接种回流污泥实现BAF一体化自养脱氮工艺[J]. 化工学报, 2017,68(5):2081-2088. Yang Q, Zhou T, Liu X H, et al. Implementation of integrated autotrophic nitrogen removal system at normal temperature by returned sludge[J]. CIESC Journal, 2017,68(5):2081-2088.
[17]
杨长生.气水比对曝气生物滤池SND的影响[J]. 工业水处理, 2011,31(8):63-66. YANG C S. Influence of air/water ratio on the performance of SND in BAF[J]. Industrial Water Treatment, 2011,(8):63-66.
[18]
Liang Y, Li D, Zhang X, et al. Performance and influence factors of completely autotrophic nitrogen removal over nitrite(CANON) process in a biofilter packed with volcanic rocks[J]. Environmental Technology, 2015,36(8):946-953.
[19]
路俊玲,陈慧萍,肖琳.温度和氨氮浓度对水体N2O释放的影响[J]. 中国环境科学, 2019,39(1):330-335. Lu J L, Chen H P, Xiao L. Coupling effect of temperature and ammonia on N2O emission in surface water[J]. China Environmental Science, 2019,39(1):330-335.
[20]
Rathnayake L, Ishii S, Satoh H. Effects of dissolved oxygen and pH on nitrous oxide production rates in autotrophic partial nitrification granules[J]. Bioresource Technology, 2015,197:15-22.
[21]
Itokawa H, Hanaki K, Matsuo T. Nitrous oxide production in high-loading biological nitrogen removal process under low COD/N ratio condition[J]. Water Research, 2001,35(3):657-664.
[22]
Qing Y, Xiuhong L, Chengyao P, et al. N2O Production during Nitrogen Removal via Nitrite from Domestic Wastewater:Main Sources and Control Method[J]. Environmental Science & Technology, 2009,43(24):9400-9406.
[23]
Noda N, Kaneko N, Mikami M, et al. Effects of SRT and DO on N2O reductase activity in an anoxic-oxic activated sludge system[J]. Water Science & Technology, 2003,48(11/12):363-370.
[24]
张铃敏,常青龙,史勤,等. CANON工艺短程硝化恢复调控及微生物种群结构变化[J]. 中国环境科学, 2019,39(6):2354-2360. Zhang L M, Chang Q L, Shi Q, et al. The recovery regulation of a CANON system and variations in the microbial community[J]. China Environmental Science, 2019,39(6):2354-2360.
[25]
Zhou X, Liu X, Huang S, et al. Total inorganic nitrogen removal during the partial/complete nitrification for treating domestic wastewater:Removal pathways and Main influencing factors[J]. Bioresource Technology, 2018,256:285-294.
[26]
Yang Q, Liu X, Peng C, et al. N2O Production during Nitrogen Removal via Nitrite from Domestic Wastewater:Main Sources and Control Method[J]. Environmental Science & Technology, 2009, 43(24):9400-9406.
[27]
Noda N, Kaneko N, Milkami M, et al. Effects of SRT and DO on N2O reductase activity in an anoxic-oxic activated sludge system[J]. Water Science and Technology, 2003,48(11/12):363-370.
[28]
刘涛,李冬,曾辉平,等.常温下CANON反应器中功能微生物的沿程分布[J]. 哈尔滨工业大学学报, 2012,44(10):22-27. Liu T, Li D, Zeng H P, et al. Distribution of functional bacteria alone bio-filter of CANON reactor at room temperature[J]. Journal of Harbin Institute of Technology, 2012,44(10):22-27.
[29]
Cema G, P?aza E, Trela J, et al. Dissolved oxygen as a factor influencing nitrogen removal rates in a one-stage system with partial nitritation and Anammox process[J]. Water Science & Technology, 2011,64(5):1009-1015.
[30]
Park H D, Wells G F, Bae H, et al. Occurrence of Ammonia-Oxidizing Archaea in Wastewater Treatment Plant Bioreactors[J]. Applied and Environmental Microbiology, 2006,72(8):5643-5647.
[31]
Hu M P, Chen D J, Dahlgren R A. Modeling nitrous oxide emission from rivers:a global assessment[J]. Global Change Biology, 2016,22(11):3566-3582.
[32]
Wunderlin P, Lehmann M F, Siegrist H, et al. Isotope Signatures of N2O in a Mixed Microbial Population System:Constraints on N2O Producing Pathways in Wastewater Treatment[J]. Environmental Science & Technology, 2013,47(3):1339-1348.
[33]
Frame C H, Casciotti K L. Biogeochemical controls and isotopic signatures of nitrous oxide production by a marine ammonia-oxidizing bacterium[J]. Biogeosciences, 2010,9(7):2695-2709.