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水力剪切力对厌氧反应器启动的影响 被引量:8

Effects of Hydrodynamic Force on Start-up of Anaerobic Reactor
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摘要 升流式厌氧反应器以絮状污泥为种泥启动,启动过程主要关注COD去除率的提高以及污泥颗粒化的情况.污泥颗粒化过程包括"成核"以及"在核基础上成熟"2个步骤,"成核"作为颗粒化的起点尤为重要.本实验运用课题组建立的定量方法,研究了在低、中、高水力剪切力条件下的絮状污泥的成核过程.在成核过程中,污泥平均粒径(average sludge diameter,ASD)、含核率(nucleus ratio,NR)都与运行时间明显线性相关,ASD的增长速率分别为0.40、0.51和0.41μm.d-1.中等水力条件下污泥的成核速度最快,相应的剪切速率为8.28 s-1,液相和气相上升流速分别为2.66和0.24 m/h.高水力剪切力下,污泥的COD去除率增长快.同时污泥去除能力与污泥性质密切相关,在试验条件下,ASD的增长速率与COD去除率达到92%的快慢是一致的. The keystones of the start-up of upflow anaerobic reactor with floeeulent sludge as seed include the improvement of COD removal and sludge granulation. The anaerobic sludge granulation consists of two steps, namely nucleation and maturation upon nuclei. The nucleation as the starting point is of particular importance. In this paper, the nucleation of floeculent sludge as seed under low, medium and high hydrodynamic shear conditions is studied with an original quantitative method. The average sludge diameters (ASD) or nucleus ratios show satisfactory linear correlations with the operation time during the nucleation and the average augmentation rate of ASD of 0.40, 0. 51 and 0.41μm · d^-1 respectively. The nucleation under the medium shear conditions of shear rate of about 8.28 s ^-1 which is corresponding to the superficial liquid and gas velocities of 2.66 and 0.24 m/h develops fastest. High hydrodynamic shear conditions enhance the improvement of COD removal of reactor. In this study the increase rate of ASD and the improvement rate of COD removal to 92% of sludge show consistent trend.
出处 《环境科学》 EI CAS CSCD 北大核心 2010年第2期368-372,共5页 Environmental Science
基金 国家自然科学基金项目(50308013,50678090) 霍英东基金优选项目(114020) 美国美铝基金项目
关键词 水力剪切力 启动 絮状污泥 厌氧颗粒化 成核 hydrodynamic shear force start-up floeculent sludge anaerobic granulation nucleation
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参考文献25

  • 1贺延龄..废水的厌氧生物处理[M],1998.
  • 2卢刚,郑平.废水生物处理中的污泥颗粒化[J].东北农业大学学报,2004,35(2):249-253. 被引量:13
  • 3Liu Y, Tay J H. The essential role of hydrodynamic shear force in the formation of biofilm and granular sludge [ J ]. Water Research, 2002,36 : 1653-1665. 被引量:1
  • 4Schmidt J E. Ahfing B K. Granular sludge formation in upflow anaerobic sludge blanker ( UASB ) reactors [ J ]. Biotechnol Bioeng, 1996, 49(3) : 229-246. 被引量:1
  • 5Wright P C, Raper J A. A review of some parameters involved in fluidized bed bioreactors[ J]. Chem Eng Technol, 1996, 19( 1 ) : 50-64. 被引量:1
  • 6Alphenaar P A, Visser A, Lettinga G. The effects of liquid upflow velocity and hydraulic retention time on granulation in UASB reactors treating wastewater with a high sulphate content [ J]. Bioresour Technol, 1993, 43 : 249-258. 被引量:1
  • 7O'Flaherty V, Lens P N, de Beer D, et al. Effect of feed composition and upflow velocity on aggregate characteristics in anaerobic upflow reactors[J]. Appl Microbiol Biotechnol, 1997, 47 : 102-107. 被引量:1
  • 8Hulshoff Pol L W, Heijnekamp K, Lettinga G. The selection pressure as a driving force behind the granulation of anaerobic sludge: microbiology and technology [ M]. The Netherlads: Pudoc Wageningen, 1988. 153-161. 被引量:1
  • 9Arcand Y, Guiot S R, Desrochers M. Impact of the reactor hydrodynamics and organic loading on the size and activity of anaerobic granules [J]. Chem Eng, 1994, 56( 1 ) : B23-B35. 被引量:1
  • 10Habets L H A, Engelaar A J H H, Groeneveld N. Anearobic treatment of inuline effluent in an Internal Circulation Reactor [J]. Water Sci Technol, 1997, 35 (10) : 189-197. 被引量:1

二级参考文献51

  • 1胡林林,王建龙,文湘华,杨宁,钱易.SBR中厌氧颗粒污泥向好氧颗粒污泥的转化[J].环境科学,2004,25(4):74-77. 被引量:31
  • 2方亮,张丽丽,蔡伟民.活性污泥胞外多聚物提取方法的比较[J].环境科学与技术,2006,29(3):46-47. 被引量:28
  • 3Lettinga G, Pette K C, de vletter R, et al. Anaerobic Treatment of Beet Sugar Wastewater on Semi-teehnical Scale [ M ]. The Netherlands Amsterdam: 1977. 被引量:1
  • 4Lettinga G, van Velsen A F M, Hobma S W, et al. Use of the upflow sludge bankct (USB) reactor concept for biologlcal waste water treatment especially for anaerobic treatment [J]. Biotech and Bioeng, 1980, 22(4): 699-734. 被引量:1
  • 5Wiegant W M. The ‘spaghetti theory' on anaerobic sludge formation, or the inevitability of granulation[ A ]. In: Lettinga G, Zehnder A J B, Grotenhuis J T C, et al, eds. Granular Anaerobic Sludge:Microbiology and Technology [ C ]. The Netherlands: Pudoc. Wageningen, 1988. 146-152. 被引量:1
  • 6Hulshoff Pol pressure as a Microbiology Wageningen, L W, Heijnekamp K, Lettinga G. The selection driving force behind the granulation of anaerobic sludge. and Technology [ M ]. The Netherlads: Pudoc. 1988. 153-161. 被引量:1
  • 7MacLeod F A, Guiot S R, Costerton J W. Layered structure of bacterial aggregates produced in an upflow anaerobic sludge bed and filter reactor [ J]. Applied Environmental Microbiology, 1990, 56 (6) : 1598-1607. 被引量:1
  • 8Guiot S R, Pauss A, Costerton J W. A structured model of the anaerobic granules consortium [J]. Water Sci Technol, 1992, 25(7- 8) : 1-10. 被引量:1
  • 9Teo K C, Xu H L, Tay J H. Molecular mechanism of granulation-Ⅱ: proton translocating activity [J]. J Environ Eng, 2000, 126(5): 411-418. 被引量:1
  • 10Tay J H, Xu H L, Teo K C. Molecular mechanism of granulation-Ⅰ: H + translocation-dedydration theory [J]. J Environ Eng, 2000, 126 (5) : 411-418. 被引量:1

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