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ABR耦合CSTR一体化工艺好氧颗粒污泥亚硝化性能调控及稳态研究
引用本文:巫恺澄,吴鹏,沈耀良,李月寒,王建芳,徐乐中.ABR耦合CSTR一体化工艺好氧颗粒污泥亚硝化性能调控及稳态研究[J].环境科学,2015,36(11):4195-4201.
作者姓名:巫恺澄  吴鹏  沈耀良  李月寒  王建芳  徐乐中
作者单位:苏州科技学院环境科学与工程学院, 苏州 215009;江苏省水处理技术与材料协同创新中心, 苏州 215009;苏州科技学院环境科学与工程学院, 苏州 215009;江苏省水处理技术与材料协同创新中心, 苏州 215009;苏州科技学院环境科学与工程学院, 苏州 215009;江苏省水处理技术与材料协同创新中心, 苏州 215009;苏州科技学院江苏省环境科学与工程重点实验室, 苏州 215009;苏州科技学院环境科学与工程学院, 苏州 215009;江苏省水处理技术与材料协同创新中心, 苏州 215009;苏州科技学院环境科学与工程学院, 苏州 215009;江苏省水处理技术与材料协同创新中心, 苏州 215009;苏州科技学院江苏省环境科学与工程重点实验室, 苏州 215009;苏州科技学院环境科学与工程学院, 苏州 215009;江苏省水处理技术与材料协同创新中心, 苏州 215009;苏州科技学院江苏省环境科学与工程重点实验室, 苏州 215009
基金项目:江苏省高校自然科学研究重大项目(12KJA610002); 苏州市环境保护科技项目(B20130502); 江苏省高校优势学科建设工程项目; 环境工程江苏省重点专业类项目
摘    要:本研究将厌氧折流板反应器(ABR)末端两隔室分别改为曝气池与沉淀池,使其成为厌氧耦合好氧一体化工艺,探索连续流条件下好氧颗粒污泥亚硝化实现条件.分别在厌氧区和好氧区接种厌氧颗粒污泥和好氧颗粒污泥,控制好氧区沉淀时间为1 h,好氧区C/N比由1逐渐降低至0.4,并逐步提高进水氨氮容积负荷由0.89 kg·(m3·d)-1提高至2.23 kg·(m3·d)-1].经45 d的运行,在好氧区成功培养出成熟的亚硝化颗粒污泥,其外观呈黄色,结构密实、边缘清晰,出水亚硝酸盐积累率稳定在80%左右.游离氨(FA)和游离亚硝酸(FNA)共同抑制作用是实现稳定亚硝酸盐积累的关键因素.运行初期部分好氧颗粒污泥出现解体现象,好氧区产生大量絮体;但后期絮体逐步转化为小粒径颗粒污泥,表明一定数量的有机碳源有利于絮体颗粒化,而大量富集慢速生长的硝化细菌对颗粒的稳定维持起重要作用.

关 键 词:连续流  亚硝化颗粒污泥  游离氯  游离亚硝酸  稳定性  颗粒化
收稿时间:2015/5/18 0:00:00
修稿时间:7/2/2015 12:00:00 AM

Research on Cultivation and Stability of Nitritation Granular Sludge in Integrated ABR-CSTR Reactor
WU Kai-cheng,WU Peng,SHEN Yao-liang,LI Yue-han,WANG Jian-fang and XU Yue-zhong.Research on Cultivation and Stability of Nitritation Granular Sludge in Integrated ABR-CSTR Reactor[J].Chinese Journal of Environmental Science,2015,36(11):4195-4201.
Authors:WU Kai-cheng  WU Peng  SHEN Yao-liang  LI Yue-han  WANG Jian-fang and XU Yue-zhong
Institution:School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;Jiangsu Collaborative Innovation Center of Technology and Material of Water Treatment, Suzhou 215009, China;School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;Jiangsu Collaborative Innovation Center of Technology and Material of Water Treatment, Suzhou 215009, China;School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;Jiangsu Collaborative Innovation Center of Technology and Material of Water Treatment, Suzhou 215009, China;Jiangsu Key Laboratory of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;Jiangsu Collaborative Innovation Center of Technology and Material of Water Treatment, Suzhou 215009, China;School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;Jiangsu Collaborative Innovation Center of Technology and Material of Water Treatment, Suzhou 215009, China;Jiangsu Key Laboratory of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China;Jiangsu Collaborative Innovation Center of Technology and Material of Water Treatment, Suzhou 215009, China;Jiangsu Key Laboratory of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou 215009, China
Abstract:The last two compartments of the Anaerobic Baffled Reactor (ABR) were altered into aeration tank and sedimentation tank respectively to get an integrated anaerobic-aerobic reactor, using anaerobic granular sludge in anaerobic zone and aerobic granular sludge in aerobic zone as seed sludge. The research explored the condition to cultivate nitritation granular sludge, under the condition of continuous flow. The C/N rate was decreased from 1 to 0.4 and the ammonia nitrogen volumetric loading rate was increased from 0.89 kg ·(m3 ·d)-1 to 2.23 kg ·(m3 ·d)-1 while the setting time of 1 h was controlled in the aerobic zone. After the system was operated for 45 days, the mature nitritation granular sludge in aerobic zone showed a compact structure and yellow color while the nitrite accumulation rate was about 80% in the effluent. The associated inhibition of free ammonia (FA) and free nitrous acid (FNA) dominated the nitritation. Part of granules lost stability during the initial period of operation and flocs appeared in the aerobic zone. However, the flocs were transformed into newly generated small particles in the following reactor operation, demonstrating that organic carbon was benefit to granulation and the enrichment of slow-growing nitrifying played an important role in the stability of granules.
Keywords:continuous flow  nitritation granular sludge  free ammonia (FA)  free nitrous acid (FNA)  stability  granulation
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