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内循环三相好氧生物流化床处理糖业废水实验研究 被引量:5

Experimental Study on an Inner-loop Three-phase Biological Fluidized Reactor for Treatment of Wastewater from Sugar Industry
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摘要 采用人工合成的多孔高分子颗粒作为微生物载体,利用内循环好氧生物流化床对不同工段的糖业废水进行连续处理。结果表明,反应器能很好降解各工段废水,CODCr平均去除率达到85%以上,当水样BOD/CODCr(B/C)值高于0.5时,出水CODCr达到80 mg/L以下,在水样B/C值为0.4时,出水CODCr能稳定在110 mg/L左右;反应器表现出较好的生物脱氮能力,其中氨氮去除率达到80%左右。同时,对反应器的抗冲击负荷能力和停留时间分布进行了实验,结果分析表明,反应器对进水CODCr负荷冲击有良好的适应性,这一良好的抗负荷冲击能力一方面源自生物膜的固定化,另一方面在于反应器内混合充分,传质效率提高且液相稀释扩散作用显著。 The biodegradation of wastewater from sugar industry in a three phase biological fluidized reactor was investigated.The reactor was continuously fed with wastewaters from different workshop sections.The results demonstrated that the average COD Cr removal efficiency was above 85%.When the BOD/CODCr(B/C) of the wastewater is above 0.5,the effluent CODCr is below 80 mg/L and when the B/C is 0.4,COD Cr in effluent is steadily around 110 mg/L.The performance of biodegradation of nitrogen was proved to be effective and the reduction rate of NH3-N is around 80%.Meanwhile,the resistance capability of the reactor to impact load and the RTD of the reactor were investigated through experiments.Based on the analysis of the results,the reactor was resisted well with the impact variance of the CODCr load in the influent.The capability of resistance to impact load comes from,on one side,the immobilization of biofilms,for another,the dilution effect of liquid due to the sufficient mixing extent in the reactor.
出处 《四川大学学报(工程科学版)》 EI CAS CSCD 北大核心 2011年第5期185-190,共6页 Journal of Sichuan University (Engineering Science Edition)
关键词 生物流化床 好氧处理 糖业废水 biological fluidized reactor aerobic treatment sugar industrial wastewater
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  • 1谢珊,李小明,曾光明,杨国靖,杨麒.SBR系统中好氧颗粒污泥脱氮特性研究[J].中国环境科学,2004,24(3):355-359. 被引量:21
  • 2缪燕江,孙宁川,杨家江.制糖废水用于农田灌溉的效果研究[J].干旱环境监测,2004,18(3):163-165. 被引量:8
  • 3贾剑晖.氨氮废水处理过程中的好氧反硝化研究[J].南平师专学报,2004,23(2):70-74. 被引量:10
  • 4周平,钱易.内循环生物流化床反应器的理论分析[J].环境科学,1995,16(2):88-90. 被引量:17
  • 5漆德瑶 肖明耀 等.理化分析数据处理手册[M].北京:中国计量出版社,1999..
  • 6H. K. Huang,S. K. Tseng.Nitrate reduction by Citrobacter diversus under aerobic environment[J]. Applied Microbiology and Biotechnology . 2001 (1)
  • 7E. B. Muller,A. H. Stouthamer,H. W. Verseveld.Simultaneous NH3 oxidation and N2 production at reduced O2 tensions by sewage sludge subcultured with chemolithotrophic medium[J]. Biodegradation . 1995 (4)
  • 8L. A. Robertson,J. G. Kuenen.Aerobic denitrification — old wine in new bottles?[J]. Antonie van Leeuwenhoek . 1984 (5-6)
  • 9Munch E V,Pant L,Jary K,et al.Simultaneous nitrification anddenitrification in bench-scale sequencing batch reactors. Water Resources Research . 1996
  • 10Scholten E,Lukow T,Auling G,et al.Thauera mechernichensissp nov:an aerobic denitrifier froma leachate treatment plant. Int JSyst Bacteriol . 1999

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  • 1王文华,沈娟,徐志刚,束忠明.气升式内环流反应器的气含率研究[J].现代化工,2007,27(z1):325-328. 被引量:6
  • 2刘梦溪,卢春喜,储凌,时铭显.中心气升式三相强化环流反应器内气含率分布的理论分析[J].高校化学工程学报,2005,19(3):332-337. 被引量:8
  • 3陈再新,费黎明,范镇,吕德伟.气液环流反应器中基于大、小两类气泡的气相返混模型和气液传质特性[J].化学反应工程与工艺,1997,13(1):58-64. 被引量:3
  • 4韦朝海,李磊.底隙设置挡板内循环流化床水力特性分析[J].化工学报,2007,58(10):2480-2484. 被引量:11
  • 5Moradi S, Rajabi Z, Mohammadi M, et al. 3 Dimensional Hydrodynamic Analysis of Concentric Draft Tube Airlift Reactors with Different Tube Diameters [J]. Math. Comput. Model., 2013, 57(5): 1184-1189.
  • 6Chisti M Y, Halard B, Moo-Young M. Liquid Circulation in Airlift Reactors [J]. Chem. Eng. Sci., 1988, 43(3): 451-457.
  • 7Luo L J, Liu F N, Xu Y Y, et al. Hydrodynamics and Mass Transfer Characteristics in an Internal Loop Airlift Reactor with Different Spargers [J]. Chem. Eng. J., 2011, 175(22): 494-504.
  • 8Livingston A G, Zhang A F. Hydrodynamics Behavior of Three-phase (Gas-Liquid-Solid) Airlift Reactors [J]. Chem. Eng. Sci., 1993, 48(9): 1641-1654.
  • 9Prieske H, Drews A, Kraume M. Prediction of the Circulation Velocity in a Membrane Bioreactor [J]. Desalination, 2008, 231(1): 219-226.
  • 10Behzadian F, Yerushalmi L, Alimahmoodi M, et al. Hydrodynamic Characteristics and Overall Volumetric Oxygen Transfer Coefficient of a New Multi-environment Bioreactor [J]. Bioprocess and Biosystems Engineering, 2013, 36(8): 1043-1052.

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