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运行模式对好氧颗粒污泥处理低碳氮比城镇废水的特性研究 被引量:4

Study on the Characteristics of Aerobic Granular Sludge in the Treatment of Urban Wastewater with Low Carbon Nitrogen Ratio
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摘要 为探究不同运行模式对好氧颗粒污泥(AGS)培养及处理低C/N城镇废水的影响,构建了两个有效体积为5.0 L的反应器,在中温条件下比较了完全好氧(R1)及多级厌氧/好氧交替(R2)对AGS及处理性能的影响。结果表明,稳定运行时,R2内MLSS含量更高,可至5346~5462 mg/L,沉降性好,SVI低至62.5~65.6 mL/g,0.3~0.6 mm粒径分布占比高达56.6%。在污染物去除方面,R2内COD去除率可高达92.5%~96.7%,而对NH_(4)^(+)-N去除方面,两反应器之间差异不明显。R2内PO_(4)^(3-)-P出水质量浓度低至0.66~1.16 mg/L,去除率高达89.5%~91.3%,高于R1。微生物群落分析表明,Saccharibacteria和Proteobacteria是主要的微生物,R2内Proteobacteria和Bacteroidetes的相对丰度分别高达35.21%和10.51%高于R1组别,这与R2展现出较好的脱氮除磷效率相一致。 To investigate the effects of different operation modes on aerobic granular sludge(AGS)culture and treatment of low C/N urban wastewater,two reactors with an effective volume of 5.0 L were constructed.The effects of complete aerobic(R1)and multistage anaerobic/aerobic alternation(R2)on AGS and treatment performance were compared at medium temperature.The results showed that under stable operation,the MLSS content in R2 was higher,up to 5346~5462 mg/L.Superior sedimentation was obtained with as low as 62.5~65.6 mL/g of SVI,and the particle size distribution of 0.3~0.6 mm accounted for 56.6%.In terms of pollutant removal,the COD removal efficiency in R2 could be as high as 92.5%~96.7%,while in terms of NH_(4)^(+)-N removal,there was no obvious difference between the two reactors.The effluent concentration of PO_(4)^(3-)-P in R2 was as low as 0.66~1.16 mg/L,and the removal efficiency was as high as 89.5%~91.3%,higher than that in R1.Microbial community analysis showed that saccharibacteria and Proteobacteria were the main microorganisms.The relative abundance of Proteobacteria and Bacteroidetes in R2 were as high as 35.21%and 10.51%respectively,which were higher than those in R1 group,consistent with R2 with better nitrogen and phosphorus removal efficiency.
作者 周寅飞 董薇 肖子瑞 ZHOU Yinfei;DONG Wei;XIAO Zirui(Yangzhou Industrial Vocational and Technical College,Yangzhou 225127,China;Nanjing Water Supply Corporation,Nanjing 210008,China)
出处 《水处理技术》 CAS CSCD 北大核心 2022年第7期117-120,130,共5页 Technology of Water Treatment
基金 教育部职业教育石油化工技术专业教学资源库(SYHGJS2020-03)。
关键词 颗粒污泥 低C/N废水 运行模式 脱氮除磷 granular sludge low C/N wastewater operation mode nitrogen and phosphorus removal
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  • 1朱亮,徐向阳,郑昱.序批式气提生物反应器(SABR)处理氯苯胺类有机废水好氧污泥颗粒化研究[J].环境科学学报,2005,25(11):1448-1456. 被引量:18
  • 2高景峰,周建强,彭永臻.处理实际生活污水短程硝化好氧颗粒污泥的快速培养[J].环境科学学报,2007,27(10):1604-1611. 被引量:30
  • 3Abma W R,Schultz C E,Mulder J W, ei al. 2007. Full-scale granularsludge Anammox process [J]. Water Science and Technology, 55(8/9) : 27-33.
  • 4Anthonisen A C, Loehr R C,Prakasam TBS, et al. 1976. Inhibition ofnitrification by ammonia and nitrous acid [ J ]. Journal WaterPollution Control Federation, 48 (5) : 835-852.
  • 5APHA. 1995. Standard Method for the Examination of Water and Wastewater ( 19th edition ) [ M ]. Washington, DC: American PublicHealth Association.
  • 6Bassin J P, Kleerebezem R,Rosado AS, et al. 2012. Effect of differentoperational conditions on biofilm development,nitrification,andnitrifying microbial population in raoving-bed biofilm reactors [ J].Environment Science and Technolgy, 46 (3) : 1546-1555.
  • 7Fux C, Boehler M,Huber P,et al. 2002. Biological treatment ofammonium-rich wastewater by partial nitritation and subsequentanaerobic ammonium oxidation ( anammox) in a pilot plant [ J ].Journal of biotechnol, 99(3) :295-306.
  • 8Hellinga C, Schellen A A J C, Mulder J W, e( al. 1998. The SHARONprocess : an innovative method for nitrogen removal from ammoniumrich wastewater [ J]. Water Science and Technology, 37 (9):135-142.
  • 9Khin T, Annachhatre A P. 2004. Novel microbial nitrogen removalprocesses [J]. Biotechnology Advances,22(7) :519-532.
  • 10Kwiatkowska A C,Baryia I W. 2011. Nitrifying granules cultivation in asequencing batch reactor at a low organics-to-total nitrogen ratio inwastewater [J]. Folia Microbiol, 56 (3) : 201 -208.

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