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SBR实现选择性硝化过程及动力学研究
引用本文:钱光磊,谢陈鑫,滕厚开,张艳芳,陆彩霞.SBR实现选择性硝化过程及动力学研究[J].环境科学学报,2016,36(7):2422-2427.
作者姓名:钱光磊  谢陈鑫  滕厚开  张艳芳  陆彩霞
作者单位:中海油天津化工研究设计院, 国家工业水处理工程技术研究中心, 天津 300131,中海油天津化工研究设计院, 国家工业水处理工程技术研究中心, 天津 300131,中海油天津化工研究设计院, 国家工业水处理工程技术研究中心, 天津 300131,中海油天津化工研究设计院, 国家工业水处理工程技术研究中心, 天津 300131,中海油天津化工研究设计院, 国家工业水处理工程技术研究中心, 天津 300131
基金项目:国家科技支撑计划(No.2014BAE06B00)
摘    要:采用序批式生物反应器(SBR)处理模拟氨氮废水,考察了SBR体系中硝化过程中氮组分和溶解氧变化规律,并对硝化动力学进行了研究.结果表明,在低溶解氧下,体系出现亚硝态氮积累;在序批式反应体系中的硝化反应呈现三阶段,即零级反应段、混合反应段和一级反应段,其硝化特性符合Monod动力学方程;根据SBR实现选择性硝化过程控制方法,实现了SBR选择性亚硝化启动,该体系氨氮出水1 mg·L~(-1),氨氮负荷达0.45 kg·kg~(-1)·d~(-1)(以每kg MLSS中的NH_4~+-N量(kg)计),亚硝态氮累积率达95%左右.

关 键 词:选择性硝化  SBR  动力学  过程控制
收稿时间:2015/9/17 0:00:00
修稿时间:2015/11/22 0:00:00

The kinetics of selective nitrification process in a sequencing batch reactor
QIAN Guanglei,XIE Chenxin,TENG Houkai,ZHANG Yanfang and LU Caixia.The kinetics of selective nitrification process in a sequencing batch reactor[J].Acta Scientiae Circumstantiae,2016,36(7):2422-2427.
Authors:QIAN Guanglei  XIE Chenxin  TENG Houkai  ZHANG Yanfang and LU Caixia
Institution:National Research Center of Industrial Water Treatment Engineering and Technology, CNOOC Tianjin Chemical Research and Design Institute, Tianjin 300131,National Research Center of Industrial Water Treatment Engineering and Technology, CNOOC Tianjin Chemical Research and Design Institute, Tianjin 300131,National Research Center of Industrial Water Treatment Engineering and Technology, CNOOC Tianjin Chemical Research and Design Institute, Tianjin 300131,National Research Center of Industrial Water Treatment Engineering and Technology, CNOOC Tianjin Chemical Research and Design Institute, Tianjin 300131 and National Research Center of Industrial Water Treatment Engineering and Technology, CNOOC Tianjin Chemical Research and Design Institute, Tianjin 300131
Abstract:The changes of nitrogen components and dissolved oxygen (DO) in nitrification process were investigated in a sequencing batch reactor (SBR) treating simulated ammonia wastewater. Besides, the kinetics of nitrification was also studied. The results show that a steady nitrite accumulation could be obtained at a low DO concentration. Moreover, the process of nitrification in the SBR presented three stages: the zero-order reaction period, the mixed-reaction period and the first-order reaction period. The nitrification follows the Monod kinetics equation. In addition, an ammonia concentration lower than 1 mg·L-1, an ammonia nitrogen loading of 0.45 kgNH+4-N·kgMLSS-1·d-1 and 95% oxidation of ammonia to nitrite were achieved in the SBR after the start of shortcut nitrification depending on the implementation of selective nitrification process control.
Keywords:selective nitrification  SBR  kinetics  process control
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