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SBBR的原位生物解偶联污泥减量系统的构建 被引量:3

Construction of Sludge Reduction System with In-situ Biological Uncoupling in SBBR
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摘要 通过对SBBR反应器充氧方式的调控来构建原位生物解偶联污泥减量系统,考察了充氧方式对SBBR反应器污泥产量和处理效能的影响。结果表明,在水温为25℃、挂膜密度为45%、负荷为1 kgCOD/(m3.d)、DO为5 mg/L的条件下,采用曝气30 min/停曝30 min的充氧方式能强化生物膜中的生物解偶联作用,构建出原位生物解偶联系统,污泥产率小,并且出水水质达标。当反应器分别采用曝气30 min/停曝30 min、曝气15 min/停曝15 min和连续曝气时,其平均污泥产率依次为0.03、0.07和0.08 kgMLSS/(kgCOD.d),与传统活性污泥法相比,其污泥产率分别减少了90%、77%和73%。 A sludge reduction system with in-situ biological uncoupling was constructed by controlling the aeration mode in SBBR. The influence of aeration mode on sludge yield and treatment efficiency in SBBR was investigated. The results show that under the conditions of temperature of 25 ℃, biofilm density of 45% , organic loading of 1 kgCOD/( m3 · d) and DO of 5 rag/L, the aeration mode of 30 rain aeration/30 min non-aeration can enhance biological uncoupling effect in the biofihn. The constructed in- situ biological uncoupling system has low sludge yield and enables the effluent to meet the discharge standard. When the aeration modes are 30 min aeration/30 rain non-aeration, 15 min aeration/15 rain non-aeration, and continuous aeration respectively, the average sludge yields are 0. 03, 0.07 and0. 08 kgMLSS/(kgCOD · d) respectively, and the sludge yields are reduced by 90% , 77% and 73% respectively compared with traditional activated sludge process.
出处 《中国给水排水》 CAS CSCD 北大核心 2011年第13期1-4,共4页 China Water & Wastewater
基金 国家水体污染控制与治理科技重大专项(2008ZX07315-005)
关键词 SBBR 充氧方式 污泥减量 生物解偶联 SBBR aeration mode sludge reduction biological uncoupling
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参考文献6

  • 1Strand S E, Harem G N,Stensel H D. Activated sludge yield reduction using chemical uncouplers [ J ]. Water En- viron Res,1999,71 (4) :454 -458.
  • 2Chen G H,Mo H K,Liu Y. Utilization of a metabolic un- coupler,3 ,3' ,4' ,5-tetrachlorosalicylanilide (TCS) to re- duce sludge growth in activated sludge culture [ J ]. Water Res,2002,36 ( 8 ) : 2077 - 2083.
  • 3Low E W,Chase H A, Milner M G,et al. Uncoupling of metabolism to reduce biomass production in the activated sludge process [ J ]. Water Res, 2000,34 ( 12 ) : 3204 - 3212.
  • 4Low E W, Chase H A. The use of chemical uncouplers for reducing biomass production during biodegradation [ J ]. Water Sci Technol, 1998,37 (4/5) : 399 - 402.
  • 5Chudoba P, Chudoba J, Capdeville B. The aspect of ener- getic uncoupling of microbial growth in the activated sludge process: OSA system [ J ]. Water Sci Technol, 1992,26 ( 9/10) : 2477 - 2480.
  • 6梁鹏,黄霞,钱易,丁国际.污泥减量化技术的研究进展[J].环境污染治理技术与设备,2003,4(1):44-52. 被引量:153

二级参考文献59

  • 1金成清.原生动物在反应器中的增长速率与功能[J].沈阳建筑工程学院学报,1996,12(4):464-468. 被引量:4
  • 2张绍园.膜分离与生物降解组合工艺处理受污染水研究:博士论文[M].北京:中国科学院生态环境研究中心,2000.19—52.
  • 3Strachan L F,Freitas dos Santos L M,Leak D J..Minimisation of biomass in an extractive membrane bioreactor..Wat Sci Tech,,1996,,34(5—6)::273—280..
  • 4Hamoda M F,Al-attar I M S..Effects of high sodium chloride concentrations on activated sludge treatment..Wat Sci Tech,,1995,,31(9)::61—72..
  • 5Abbassi B,Dullstein S,Rabiger N..Minimization of excess sludge production by increase of oxygen concentration in activated sludge flocs:experimental and theoreticalapproach..Wat Res,,2000,,34(1)::139—146..
  • 6Mark C M,Loosdrecht V,Henze M..Maintenance,endogeneous respiration,lysis,decay and predation..Wat Sci Tech,,1999,,39(1)::107-117..
  • 7Yasui H,Shibata M..An innovative approach to reduce excess sludge production in the activated sludge process ..Wat Sci Tech,,1994,,30(9)::11—20..
  • 8Sakai Y,Fukase T,Yasui H..An activated sludge process without excess sludge production.. Wat.Sci.Tech.,,1997,,36(11)::163—170..
  • 9Lim H N,Choi H Hwang T M,Kang J W..Characterization of ozone decomposition in a soil slurry:kinetics,mechanism..Wat Res,,2002,,36(1)::219—229..
  • 10Weemaes M,Grootaerd H,Simoens F..Anaerobic digestion of ozonized biosolids..Wat Res,,2000,,34(8)::2330--2336..

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