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基于FLUENT的微细赤铁矿颗粒絮凝过程的数值模拟

Numerical simulation of the flocculation process of fine hematite particles based on FLUENT
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摘要 应用计算流体力学软件FLUENT对试验中不同搅拌转速下的水流流态进行三维数值模拟,以计算所得的紊动动能κ、有效能耗ε和微涡旋尺度λ作为评价絮凝是否充分的指标。通过烧杯试验和对其内水流流态的数值模拟,分析了搅拌转速对絮凝效果的影响,建立了搅拌转速同沉降率E_s、整体平均有效能耗ε和微涡旋尺度λ之间的定量关系。烧杯试验中流体为浓度2%的微细(平均粒径21.35μm)赤铁矿矿浆,絮凝剂为食用玉米淀粉。结果表明,数值计算所得的κ、ε和λ能合理解释絮凝搅拌转速对絮凝效果的影响。 The CFD (Computational Fluid Dynamics) software FLUENT is applied to 3D numerical simulation of the water flow pattern in different agitation speed under test. Calculated numerical values of the turbulent kinetic energy k the effective energy dissipation ε and microvortex scale k are defined as the criterions for evaluating the flocculation action whether it is enough or not. Through the jar test and numerical simulation of the flow pattern in it, influence of the stirring speed on the flocculation is analyzed and the quantitative relation among the stirring speed settlement ratio Es, the overall average effective energy dissipation ε and the microvortex scale k is established. The liquid used for the beaker test is of fine hematite pulp with the concentration of 2% and the average particle size of 21.35μm, while maize starch is used as flocculant. With calculated values of k, ε and k in the paper, the influence of the agitating speed on the flocculation action can be reasonably explained.
出处 《矿山机械》 北大核心 2009年第21期79-83,共5页 Mining & Processing Equipment
基金 河北省重点基础研究资助项目(08966710D) 唐山市21项重大工程项目(07130205A-1)
关键词 微细赤铁矿 絮凝 烧杯试验 数值模拟 fine hematite flocculation jar test numerical simulation
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参考文献10

  • 1宋佩娣,陈卫,周克梅.水厂混凝杯罐试验合理工况的确定[J].中国给水排水,2005,21(12):47-49. 被引量:6
  • 2Deliang Shi, J. J, McCarthy. Numerical simulation of liquid transfer between particles[J]. PowderTechnology, 2008, 184(1): 64-75.
  • 3DeSilva, IPD. Turbulence dissipation in stirred jars[J]. Journal of Engineering Mechanics, 2006, 132(11): 1260-1263.
  • 4R. B u rger, S. Evje, K. Hvistendahl Karlsen, et al. Numerical methods for the simulation of the settling of flocculated suspensions [J]. International Journal of Mineral Processing. 2000, 80(1): 91-94.
  • 5CLEASBYleasby J L. Is velocity gradient a valid tur-bulent flocculation parameter [J]. J Environ Eng Div-ASCE, 2005, 110(EES): 875-897.
  • 6周国忠,施力田,王英琛.搅拌槽内近桨区流动场的数值研究[J].高校化学工程学报,2002,16(1):17-22. 被引量:29
  • 7CLARK M M. Critique of camp and stein's RMS ve-locity gradient[J]. Environ Eng Div-ASCE, 2004,111(EE3): 741-754.
  • 8M. S. Nasser, A. E. James. Numerical simulation of the continuous thickeningofflocculated kaolinite suspensions[J]. International Journal ofMineralProcessing, 2007. 84(10): 144-147.
  • 9周国忠,王英琛,施力田.搅拌槽内三维流动场的RNG k-ε数值模拟[J].北京化工大学学报(自然科学版),2002,29(2):15-19. 被引量:21
  • 10张国娟,闵健,高正明,牛国瑞,施力田.涡轮桨搅拌槽内混合过程的数值模拟[J].北京化工大学学报(自然科学版),2004,31(6):24-27. 被引量:38

二级参考文献23

  • 1侯拴弟.搅拌槽中流体动力学模拟及实验研究[M].北京:北京化工大学,1997..
  • 2Bartels C, Breuer M, Durst F. Comparison between DNS and k-ε prediction of the flow in a vessel stirred by a Rushton turbine. In: Van den Akker H E A, Derksen J J. Proceedings of 10th European Conference on Mixing[C]. Delft: Elsevier Science B V,2000. 239~246
  • 3Revstedt J, Fuchs L, Tragardh C. Large Eddy Simulation of the Turbulent Flow in a Stirred Reactor[J]. Chem Eng Sci, 1998, 53: 4041~4053
  • 4Wu H, Patterson G K. Laser-doppler measurement of turbulent flow parameters in a stirred mixer[J]. Chem Eng Sci, 1989, 44: 2207~2221
  • 5Yakhot V, Orszag S A. RNG analysis of turbulence I:Basic theory[J]. J Sci Comput, 1986, 1: 3~51
  • 6Brucato A, Ciofalo M, Grisafi F, et al. Numerical prediction of flow fields in baffled stirred vessels: a comparison of alternative modeling approaches[J]. Chem Eng Sci, 1998, 53: 3653~3684
  • 7Rhie C M, Chow W L. A numerical study of the turbulent flow past an aerofoil with trailing edge separation[J]. AIAA J, 1983, 21: 1525~1532
  • 8Dyster K N, Koutsakos E, Jaworski Z, et al. An LDA study of the radial discharge velocities generated by a Rushton turbine: Newtonian fluid, Re≥5[J]. Trans IChemE, 1993, 71(A): 11~23
  • 9Kemoun A, Lusseyran F, Mahouast M, et al. Experimental determination of the complete Reynolds stress tensor in fluid agitated by a Rushton turbine[R]. 8th European Conference on Mixing. Cambridge. 1994. 399~406
  • 10Mahouast M, David R, Cognet G. Caracterisation des champs hydrodynamique et de concentration dans une cuve agitee standard alimentee en continu[J]. Entropie, 1987, 133: 7~17

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