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SBR工艺低溶解氧丝状菌污泥膨胀成因及控制方法 被引量:4

Filamentous Sludge Bulking Cause Analysis Under Low Dissolved Oxygen and Control Method in SBR Process
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摘要 采用序批式活性污泥(sequencing batch reactor,SBR)工艺处理低碳氮比实际生活污水,研究了低溶解氧丝状菌污泥膨胀的成因及不同运行模式对低溶解氧污泥膨胀控制效果.试验结果表明,缺氧/好氧(anoxic/oxic,A/O)工艺当溶解氧(dissolved oxygen,DO)的质量浓度ρ(DO)控制在0.5 mg/L时,发生以H.hydrossis为优势菌的丝状菌污泥膨胀.当采用SBR工艺A/O运行模式,改变有机负荷(F/M)为0.83 kg/(kg·d),ρ(DO)控制在2.0 mg/L左右时,污泥膨胀并不能有效控制,污泥体积指数(sludge volume index,SVI)一直保持在300 mL/g以上.经荧光原位杂交(fluorescence in situ hybridization,FISH)方法鉴定,优势菌种依然为H.hydrossis丝状菌,在此阶段系统总氮(total nitrogen,TN)平均去除率为31.17%,COD平均去除率为65.04%.当采用全程好氧运行模式,改变F/M为0.37 kg/(kg·d),ρ(DO)控制在2.0 mg/L左右时,能有效控制污泥膨胀,SVI下降到150 mL/g以下.在此阶段,NH+4-N去除率接近100%,出水ρ(NH+4-N)几乎为0,TN和COD的平均去除率分别上升为70.7%和73.9%.此阶段出水ρ(TN)和ρ(COD)平均值分别为18.4和46.9 mg/L,接近国家一级A排放标准. By treating real domestic sewage which is low p (C)/p (N) in sequencing batch reactor (SBR) , the cause of filamentous sludge bulking and the effect of controlling filamentous sludge bulking under low dissolved oxygen with different operation patterns were investigated. Results showed that when the dissolved oxygen (DO) value was 0.5 mg/L in anoxic/oxic process (A/O), filamentous sludge bulking happened and H. hydrossis was the dominant filamentous bacteria in filamentous bulking sludge. During A/ O pattern in SBR, sludge volume index (SVI) has maintained beyond 300 mL/g when organic loading (F/M) was 0. 83 kg/(kg-d) and the p(DO) was about 2 mg/L, the sludge bulking could not be effectively controlled. The result of fluorescence in situ hybridization (FISH) manifested that the main filamentous bacteria was also H. hydrossis filamentous bacteria. In this period, average removal rates of total nitrogen (TN) and COD were 31. 17% and 65.04% , respectively. Then during aerobic pattern, when F/M was0.37 kg/(kg d) , thep(DO) was also about 2 mg/L, the sludge bulking has been controlled effectively and SVI has remained below 150 mL/g. In this stage, the removal rate of NH4+ -N reached 100% nearly , the p(NH4+ -N)in effluent was almost 0. Average removal rates of TN and COD improved to 70.7% and 73.9% , respectively. The average p(TN) and p(COD) in effluent were 18.4 and 46.9 mg/L, respectively, close to the national level A emission standard.
出处 《北京工业大学学报》 CAS CSCD 北大核心 2013年第12期1880-1886,共7页 Journal of Beijing University of Technology
基金 青年科学基金资助项目(51108005)
关键词 序批式活性污泥法(SBR) 有机负荷(F M) 低氧污泥膨胀 H hydrossis丝状菌 荧光原位杂交(FISH) sequencing batch reactor (SBR) organic loadings (F/M) low dissolved oxygen sludgebulking H. hydrossis filamentous bacteria fluorescence in situ hybridization (FISH)
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  • 1NOVK L, LARREA L, WANNER J, et al. Non- filamentous activated sludge bulking in a laboratory scale system [J]. Water Research, 1993, 27(8): 1339-1346.
  • 2GUO Feng, ZHANG Tong. Profiling bulking and foaming bacteria in activated sludge by high through put sequencing [J]. Water Research, 2012, 46(8) : 2772-2782.
  • 3刘旭亮,彭永臻,彭赵旭,于振波,柴同志.高曝气量引发的活性污泥粘性膨胀研究[J].中国给水排水,2011,27(17):1-5. 被引量:18
  • 4Qinxue Wen,Zhiqiang Chen,Changyong Wang,Nanqi Ren.Bulking sludge for PHA production:Energy saving and comparative storage capacity with well-settled sludge[J].Journal of Environmental Sciences,2012,24(10):1744-1752. 被引量:16
  • 5张强.污水生化处理中污泥膨胀原因及控制措施的研究[J].环境与发展,2012,24(4):129-132. 被引量:1
  • 6吴昌永,彭永臻,王淑莹,刘洋,彭轶,李晓玲.A^2/O工艺的污泥膨胀及污泥特性研究[J].中国给水排水,2008,24(23):33-35. 被引量:5
  • 7GUO Jian-haa, PENG Yong-zhen, WANG Sbu-ying, et al. Stable limited filamentous bulking through keeping the competition between floc-formers and filaments in balance [ J]. Bioresource Technology, 2012, 103 ( 1 ) : 7-15.
  • 8HUET J, DRUILHE C, TREMIER A, et al. The impact of compaction, moisture content, particle size and type of bulking agent on initial physical properties of sludge- bulking agent mixtures before composting[ J]. Bioresource Technology, 2012, 114: 428-436.
  • 9GUO Jian-hua, PENG Yong-zhen, WANG Zhong-wei, et al. Control filamentous bulking caused by chlorine- resistant Type 021N bacteria through adding a biocide CTAB[J]. Water Research, 2012, 46( 19): 6531-6542.
  • 10CHUDOBA J. Control of activated sludge filamentous bulking: VI formulation of basic principle [ J]. Water Research, 1995, 19(8): 1017-1022.

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