城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能

李宁宁, 于德爽, 李津, 王晓霞, 赵丹. 城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能[J]. 环境工程学报, 2013, 7(5): 1689-1694.
引用本文: 李宁宁, 于德爽, 李津, 王晓霞, 赵丹. 城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能[J]. 环境工程学报, 2013, 7(5): 1689-1694.
Li Ningning, Yu Deshuang, Li Jin, Wang Xiaoxia, Zhao Dan. Start up of anaerobic ammonium oxidation process and nitrogen removal performance in anaerobic sequencing batch reactor for municipal sewage[J]. Chinese Journal of Environmental Engineering, 2013, 7(5): 1689-1694.
Citation: Li Ningning, Yu Deshuang, Li Jin, Wang Xiaoxia, Zhao Dan. Start up of anaerobic ammonium oxidation process and nitrogen removal performance in anaerobic sequencing batch reactor for municipal sewage[J]. Chinese Journal of Environmental Engineering, 2013, 7(5): 1689-1694.

城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能

  • 基金项目:

    国家自然科学基金资助项目(51078191,51278285)

  • 中图分类号: X703.1

Start up of anaerobic ammonium oxidation process and nitrogen removal performance in anaerobic sequencing batch reactor for municipal sewage

  • Fund Project:
  • 摘要: 采用ASBR在城市污水条件下进行厌氧氨氧化的启动与脱氮性能研究。实验接种好氧硝化污泥,在温度为(35±1)℃、HRT为24 h、pH为7.3~8.5的条件下经过130 d的培养,成功启动了厌氧氨氧化反应。实验结果表明,厌氧氨氧化反应稳定运行时,TN容积负荷平均为0.179 kg/(m3·d),NH4+-N、NO2--N和TN去除率分别达到了95.30%、91.30%和76.28%。启动期和稳定运行期NH4+-N、NO2--N去除量和NO3--N生成量的比值分别达到1:1.54:0.25和1:1.27:0.27;稳定运行期进出水pH差值由启动时的0.85下降到0.24。启动期反硝化和厌氧氨氧化反应同时存在而在稳定运行期厌氧氨氧化发展成为主导反应。MLSS和MLVSS/MLSS先减少后增加,反映了启动过程中硝化细菌、反硝化细菌的衰亡和厌氧氨氧化菌逐渐富集的过程,这与反应器的宏观运行效果相一致。
  • [1] Van de Graaf A. A., Mulder A.,Bruijn P.,et al. Anaerobic oxidation of ammonium is a biologically mediated process.Applied and Environmental Microbiology,1995, 61(4) : 1246-1251
    [2] Tal Y., Watts J. E. M., Schreier H. J. Anaerobic ammonia--oxidizing bacteria and related activity in baltmore inner harbor sedinent. Applide and Environmental Microbiology,2005,71(4):1816-1821
    [3] Mulder A., van de Graaf A. A., Robortson L., et al. Anaerobic ammonium oxidation discovered in a denitrifying fluid bed reactor. FEMS Microbiology Ecology, 1995, 16(3):177-184
    [4] Joss A., Salzgeber D., Eugster J., et al. Full-scale nitrogen removal from digester liquid with partial nitritation and anammox in one SBR. Environmental Science and Technology,2009,43(14):5301-5306
    [5] Vazquez-Padin J. R., Pozo M. J., Jarpa M. M., et al. Treatment of anaerobic sludge digester effluents by the CANON process in an air pulsing SBR. Journal of Hazardous Materials,2009,166(1):336-341
    [6] Byrne N., Strous M., Crepeau V., et al. Presence and activity of anaerobic ammonium-oxidizing bacteria at deep-sea hydrothermal vents. The ISME Journal,2009,3(1):117-123
    [7] Tang Chongjian, Zheng Ping, Wang Caihua. Suppression of anaerobic ammonium oxidizers under high organic content in high-rate Anammox UASB reactor. Bioresource Technology,2010,101(6):1762-1768
    [8] Strous M.,Pelletier E. Deciphering the evolution and metabolism of an ANAMMOX bact.Journal of Bacteriology,2008,190(2):708-717
    [9] 唐崇俭,郑平,汪彩华,等. 高负荷厌氧氨氧化EGSB反应器的运行及其颗粒污泥的ECP特性. 化工学报,2010,61(3): 732-739 Tang Chongjian, Zheng Ping, Wang Caihua, et al. Granulation and characteristics of extracellular polymers of anammox sludge in high-load EGSB reactor. CIESC Journal,2010,61(3):732-739(in Chinese)
    [10] Kimura Y., Isaka K., Kazama F.,et al. Effects of nitrite inhibition on anaerobic ammonium oxidation. Appl. Microbiol. Biotechnol., 2010, 86(1):359-365
    [11] 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, 2005
    [12] Chamchoi N., Nitisoravut S.,Schmidt J. E. Inactivation of anammox communities under concurrent operation of anaerobic ammonium oxidation(ANAMMOX) and denitrification. Bioresour. Technlo., 2008, 99(9):3331-3336
    [13] Fux C.,Boehler M.,Huber P., et al. Biological treatment of ammonium rich. wastewater by partial nitrialnit rotation and subsequent anaerobic ammonium oxidation (anammox)in a pilot plant.Biotechnol.,2002,99(3):295-306
    [14] Li Huosheng, Zhou Shaoqi, Ma Weihao,et al. Fast start-up of ANAMMOX reactor: Operational strategy and some characteristics as indicators of reactor performance. Desalination,2012,286(1):436-441
    [15] Nutchanat Chamchoi, Suwanchai Nitisoravut. Anammox enrichment from different conventional sludges. Chemosphere,2007,66(11):2225-2232
    [16] Laura van Niftrik, Willie J. C. Gddrts, Elly G. van Donselaar,et al. Combined structural and chemical analysis of the anammoxosome: A membtane-bounded intracytoplasmic compartment in anammox bzcteria. Journal of Structural Biology, 2012, 161(3):401-410
    [17] Yasuhiro Date,Kazuichi Lsaka,Hajime Lkuta,et al. Microbial diversity of anammox bacteria enriched from different types of seed sludge in an anaerobic continuous-feeding cultivation reactor. Journal of Bioscience and Bioengineering, 2009, 107(3):281-286
    [18] Alexander Galan, Veronica Molina, Bo Thamdrup, et al. Anammox bacteria and the anaerobic oxidation of ammonium in the oxygen minimum zone off northern Chile. Deep Sea Research PartⅡ:Topical Studies in Oceanography, 2009, 56(16):1021-1031
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  • 收稿日期:  2012-05-09
  • 刊出日期:  2013-05-22
李宁宁, 于德爽, 李津, 王晓霞, 赵丹. 城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能[J]. 环境工程学报, 2013, 7(5): 1689-1694.
引用本文: 李宁宁, 于德爽, 李津, 王晓霞, 赵丹. 城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能[J]. 环境工程学报, 2013, 7(5): 1689-1694.
Li Ningning, Yu Deshuang, Li Jin, Wang Xiaoxia, Zhao Dan. Start up of anaerobic ammonium oxidation process and nitrogen removal performance in anaerobic sequencing batch reactor for municipal sewage[J]. Chinese Journal of Environmental Engineering, 2013, 7(5): 1689-1694.
Citation: Li Ningning, Yu Deshuang, Li Jin, Wang Xiaoxia, Zhao Dan. Start up of anaerobic ammonium oxidation process and nitrogen removal performance in anaerobic sequencing batch reactor for municipal sewage[J]. Chinese Journal of Environmental Engineering, 2013, 7(5): 1689-1694.

城市污水条件下ASBR厌氧氨氧化的启动与脱氮性能

  • 1. 青岛大学化学化工与环境学院,青岛 266071
基金项目:

国家自然科学基金资助项目(51078191,51278285)

摘要: 采用ASBR在城市污水条件下进行厌氧氨氧化的启动与脱氮性能研究。实验接种好氧硝化污泥,在温度为(35±1)℃、HRT为24 h、pH为7.3~8.5的条件下经过130 d的培养,成功启动了厌氧氨氧化反应。实验结果表明,厌氧氨氧化反应稳定运行时,TN容积负荷平均为0.179 kg/(m3·d),NH4+-N、NO2--N和TN去除率分别达到了95.30%、91.30%和76.28%。启动期和稳定运行期NH4+-N、NO2--N去除量和NO3--N生成量的比值分别达到1:1.54:0.25和1:1.27:0.27;稳定运行期进出水pH差值由启动时的0.85下降到0.24。启动期反硝化和厌氧氨氧化反应同时存在而在稳定运行期厌氧氨氧化发展成为主导反应。MLSS和MLVSS/MLSS先减少后增加,反映了启动过程中硝化细菌、反硝化细菌的衰亡和厌氧氨氧化菌逐渐富集的过程,这与反应器的宏观运行效果相一致。

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