常温低基质厌氧氨氧化反应器启动及其稳定性

鲍林林, 赵建国, 李晓凯, 李冬, 张杰. 常温低基质厌氧氨氧化反应器启动及其稳定性[J]. 环境工程学报, 2013, 7(3): 981-986.
引用本文: 鲍林林, 赵建国, 李晓凯, 李冬, 张杰. 常温低基质厌氧氨氧化反应器启动及其稳定性[J]. 环境工程学报, 2013, 7(3): 981-986.
Bao Linlin, Zhao Jianguo, Li Xiaokai, Li Dong, Zhang Jie. Start-up and stability of Anammox bioreactor at normal temperature and low substrate concentration[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 981-986.
Citation: Bao Linlin, Zhao Jianguo, Li Xiaokai, Li Dong, Zhang Jie. Start-up and stability of Anammox bioreactor at normal temperature and low substrate concentration[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 981-986.

常温低基质厌氧氨氧化反应器启动及其稳定性

  • 基金项目:

    河南省重大公益性科研项目(081100910300)

    河南省基础与前沿技术研究计划项目(102300410195,102300410197)

  • 中图分类号: X703

Start-up and stability of Anammox bioreactor at normal temperature and low substrate concentration

  • Fund Project:
  • 摘要: 以上向流生物滤池为反应器,以实验室内氧化沟回流污泥为接种污泥,采用先培育好氧生物膜,后转为厌氧环境培育厌氧氨氧化生物膜的方式,成功实现了常温低基质浓度下厌氧氨氧化反应器的启动。控制反应器进水pH为7.50~7.80,NH4+-N为30~40 mg/L,NO2--N为35~50 mg/L,温度为20~25℃。224 d以后,反应器启动成功。在稳定运行阶段,出水亚硝氮和氨氮的平均浓度分别为1.4 mg/L和4.6 mg/L,平均去除率分别为95.3%和90.1%,去除比例为1~1.8∶1,主要集中在1.4~1.5∶1,亚硝氮和氨氮去除的容积负荷分别为104.2 mg/(L·d)和146.0 mg/(L·d)。
  • [1] Mulder A., Van de Graaf A. A., Robertson L. A., et al. Anaerobic ammonium oxidation discovered in a denitrifying fluidized bed reactor. FEMS Microbiology Ecology, 1995, 16(3): 177-183
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    [3] 沈平,左剑恶,杨洋.接种不同污泥的厌氧氨氧化反应器的启动和运行.中国沼气, 2004, 22(3):3-7 Sheng Ping,Zuo Jiane,Yang Yang.A study on start-up and operation of anaerobic ammonia oxidation reactors inoculated with different seed sludge. China Biogas, 2004, 22(3):3-7(in Chinese)
    [4] 葛林燕, 黄勇, 袁怡. 厌氧氨氧化反应器的启动运行分析.环境污染与防治, 2008, 30(5): 83-87 Ge Linyan,Huang Yong,Yuan Yi.Literature review of start-up and performance of ANAMMOX bioreactors. Environmental Pollution & Control, 2008, 30(5): 83-87(in Chinese)
    [5] 唐崇俭, 郑平, 陈建伟等. 不同接种物启动Anammox反应器的性能研究. 中国环境科学, 2008, 28(8): 683-688 Tang Chongjian,Zheng Ping,Chen Jianwei,et al.Performance of Anammox bioreactors started up with different seeding sludges. China Environmental Science, 2008, 28(8): 683-688(in Chinese)
    [6] Broda E. Two kinds of lithotrphs missing in nature. Journal of Basic Microbiology, 1977, 17(6): 491-493
    [7] Wouter R. L., van der Star, Wiebe R.Abma, et al. Startup of reactors for anoxic ammonium oxidation: Experiences from the first full-scale anammox reactor in Rotterdam. Water Research, 2007, 41(18): 4149-4163
    [8] U. van Dongen, Jetten M. S. M., C. M. van Loosdrecht. The SHARON-ANAMMOX process for treatment of ammonium rich wastewater. Water Science and Technology, 2001, 44(1): 153-160
    [9] Furukawa K., Tokitoh H., Lieu P. K. Single-stage nitrogen removal using anammox and partial nitritation(SNAP) for treatment of synthetic landfill leachate. Jpn. J. Water Treat. Biol., 2005, 41(2): 103-112
    [10] 郑平, 徐向阳, 胡宝兰. 新型生物脱氮理论与技术. 北京:科学出版社,2004
    [11] Strous M., Heijnen J. J., Kuenen J. G., et al. The sequencing batch Reactor as a power tool for the study of slowly growing anaerobic ammonium-oxidizing microorganisms. Appl. Microbiol. Biotechnol., 1998, 50(5): 589-596
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    [13] 许玫英, 方卫, 张丽娟, 等. 生物脱氮新技术在垃圾渗滤液工程化处理中的应用.环境科学, 2007, 28(3): 607-612 Xu Meiying, Fang Wei, Zhang Lijuan, et al. Application of new biological nitrogen removal technologies in full-scale treatment of landfill leachate. Environmental Science, 2007, 28(3): 607-612(in Chinese)
    [14] 张鸿郭, 周少奇. 垃圾渗滤混合液启动ANAMMOX反应器研究.工业安全与环保, 2006, 32(5): 7-9 Zhang Hongguo, Zhou Shaoqi. Study on start-up of ANAMMOX bioreactor using mixture of leachate. Industrial Safety and Environmental Protection, 2006, 32(5): 7-9(in Chinese)
    [15] 张树德, 刘欣, 郑志军, 等. 低基质质量浓度条件下ANAMMOX生物滤池脱氮效果研究.北京工业大学学报, 2009, 35(4): 504-508 Zhang Shude, Liu Xin, Zheng Zhijun,et al. Nitrogen removal efficiency of ANAMMOX biofilter at low substrate concentration. Journal of Beijing University of Technology, 2009, 35(4): 504-508(in Chinese)
    [16] 陈永, 李捷, 张树德, 等. 温度对ANAMMOX滤池的影响. 重庆大学学报(自然科学版), 2007, 30(7): 92-95 Chen Yong,Li Jie,Zhang Shude,et al.Effects of Temperature on the Performance of ANAMMOX Biofilter. Journal of Chongqing University (Natural Science), 2007, 30(7): 92-95(in Chinese)
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    [20] 唐崇俭,郑平,金仁村,等. Anammox反应器运行稳定性及其机理研究. 四川大学学报(工程科学版), 2009, 41(2): 113-119 Tang Chongjian, Zheng Ping, Jin Rencun, et al. Stability and mechanism of anammox bioreactors. Journal of Sichuan University (Engineering Science), 2009, 41(2): 113-119(in Chinese)
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出版历程
  • 收稿日期:  2011-12-15
  • 刊出日期:  2013-03-18
鲍林林, 赵建国, 李晓凯, 李冬, 张杰. 常温低基质厌氧氨氧化反应器启动及其稳定性[J]. 环境工程学报, 2013, 7(3): 981-986.
引用本文: 鲍林林, 赵建国, 李晓凯, 李冬, 张杰. 常温低基质厌氧氨氧化反应器启动及其稳定性[J]. 环境工程学报, 2013, 7(3): 981-986.
Bao Linlin, Zhao Jianguo, Li Xiaokai, Li Dong, Zhang Jie. Start-up and stability of Anammox bioreactor at normal temperature and low substrate concentration[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 981-986.
Citation: Bao Linlin, Zhao Jianguo, Li Xiaokai, Li Dong, Zhang Jie. Start-up and stability of Anammox bioreactor at normal temperature and low substrate concentration[J]. Chinese Journal of Environmental Engineering, 2013, 7(3): 981-986.

常温低基质厌氧氨氧化反应器启动及其稳定性

  • 1. 河南师范大学环境学院,黄淮水环境与污染防治教育部重点实验室,河南省环境污染 控制重点实验室,新乡 453007
  • 2. 哈尔滨工业大学市政环境工程学院,哈尔滨 150090
基金项目:

河南省重大公益性科研项目(081100910300)

河南省基础与前沿技术研究计划项目(102300410195,102300410197)

摘要: 以上向流生物滤池为反应器,以实验室内氧化沟回流污泥为接种污泥,采用先培育好氧生物膜,后转为厌氧环境培育厌氧氨氧化生物膜的方式,成功实现了常温低基质浓度下厌氧氨氧化反应器的启动。控制反应器进水pH为7.50~7.80,NH4+-N为30~40 mg/L,NO2--N为35~50 mg/L,温度为20~25℃。224 d以后,反应器启动成功。在稳定运行阶段,出水亚硝氮和氨氮的平均浓度分别为1.4 mg/L和4.6 mg/L,平均去除率分别为95.3%和90.1%,去除比例为1~1.8∶1,主要集中在1.4~1.5∶1,亚硝氮和氨氮去除的容积负荷分别为104.2 mg/(L·d)和146.0 mg/(L·d)。

English Abstract

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