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基于GAC颗粒污泥厌氧氨氧化EGSB反应器的快速启动

Quick Start-up of Anammox EGSB Reactor by Using GAC Granular Sludge
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摘要 以GAC颗粒污泥为接种污泥研究厌氧氨氧化EGSB反应器快速启动的条件及运行参数。反应器的启动在17 d内完成,总氮容积负荷达到1.62 kg/(m3·d)。采用缩短水力停留时间方式提高反应器负荷,14 d内反应器总氮容积负荷能快速升至1.45 kg/(m3·d),实验结果表明采用低基质浓度和缩短水力停留时间方式更利于厌氧氨氧化反应器的启动。第18~21 d平均产气速率为1.1 L/h,用气相色谱仪对EGSB反应器产生的气体进行分析,N2O、CO2平均体积分数分别为0.8%、0.02%,如何降低气体中N2O的浓度需要进一步研究。 The aim of this study is to explore the conditions of quick start- up and operation parameters of EGSB reactor with GAC granular sludge as the inoculation sludge. The results show that the start- up of reactor can complete in 17 days and the volume load of total nitrogen can reach 1. 62 kg /( m3·d). It can rise up to 1. 45 kg/( m3·d) within 14 days through shortening hydraulic retention time( HRT). The results also indicate that using low substrate concentration and short HRT is more helpful to the start of the anammox reactor. The average gas generation rate is 1. 1 L / h. The gases produced from EGSB reactor are analyzed by the gas chromatograph and it is found that the average content of N2 O and CO2 is 0. 8% and 0. 02% respectively. So how to reduce N2 O emission will still be a key factor for anammox application.
出处 《工业安全与环保》 北大核心 2015年第2期1-3,共3页 Industrial Safety and Environmental Protection
基金 国家自然科学基金(51108108) 广西自然科学基金(2013GXNSFCA019018) 广西高校科学技术研究项目(2013ZD031 2013ZL076) 广西矿冶与环境科学实验中心资助项目(KH2012ZD004) 广西研究生教育创新计划资助项目(YCSZ2013075) "广西危险废物处置产业化人才小高地"资助项目
关键词 GAC颗粒污泥 厌氧氨氧化 EGSB 水力停留时间 N2O GAC granular sludge anammox EGSB hydraulic retention time N2O
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  • 1刘宏娟,朱文亭,周莉莉.厌氧折流板反应器处理制药废水中试研究[J].给水排水,2008,34(S1):210-212. 被引量:3
  • 2杨洋,左剑恶,沈平,顾夏声.温度、pH值和有机物对厌氧氨氧化污泥活性的影响[J].环境科学,2006,27(4):691-695. 被引量:180
  • 3国家环境保护总局《水和废水监测分析方法》编委会.水和废水监测分析方法[M].4版.北京:中国环境科学出版社,2002:156-290.
  • 4Jin R C, Zheng P, Hu A H, et al. Performance comparison oftwo anammoxreactors: SBR end UBF[J].Chem Eng.,2008,138:224-230.
  • 5De GraaffM S, Zeeman G, Temmink H, et al. Long term partial nitritation of anaerobically treated black water and the emission of nitrous oxide[J].water Res.,2010,44(7) :2171-2178.
  • 6Iko Tsushima, Yuji Ogasawara,Tomonri Kindaichi, et al. Development of high-rate anerobic ammonium-oxidizing (anammox) biofihn reactors [J] .Water Res.,2007,41 ( 1 ): 1623 - 1634.
  • 7Van Dongen U, Jetten M S M, Van Loosdrecht M C M. The Sharon- anmmox process for treatment of ammonium rich wastewater[J]. Water Sci Technol.,2001,44(1): 153-160.
  • 8Van Loosdrecht M C M, Jetten M S M. Microbiological corrversions in nitrogenremoval[J].Water Science and Technology,1998,38:1-7.
  • 9Fux C, Boehler M, Huber P, et al. Biological treatment of ammonium- rich wastewater by partial nitritation end subsequent enerobicammonium oxidation (anammox) in a pibtplant[J].J Biotechnol.,2002,99(3 ):295-306.
  • 10S'ons M, Heijnen J J, Kuonen J G, et al. The sequencing batch reactor as a powerful tool for the study of slowly growing anaerobic ammonium- oxidizingmicrorgenisms [J].Appl Microbiol Biotechnol.,1998,50 (5): 589-596.

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