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固液搅拌槽内近壁区液相速度研究 被引量:17

Determination of liquid velocity near wall region in a solid liquid stirred tank
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摘要 在直径 4 76mm的固液搅拌槽内 ,采用自行研制的双电导电极探头对搅拌槽内距壁 0 4mm的近壁区液相速度进行了测定。平均固相体积分数v 从 1 0 %至 5 4%。实验结果表明 :固体颗粒离底悬浮最小液相速度与固液的物理性质有关 ,而与实验的操作条件无关 ;液相速度和搅拌转速在近壁上流区成正比关系 ,而在槽底区不成正比关系 ;临界均匀悬浮时 ,近壁上流区液相速度不随固相体积分数变化 ; Experiment was carried out in a cylindrical plexiglass tank of 476?mm diameter with a solid liquid system. A new type of bi electrode probe was used to measure the liquid velocity near the wall region of the tank with solid volumetric concentration(  v) from 1 0% to 5 4%.The result show that the minimum liquid velocity in the just suspension region was influenced by the properties of the solid and liquid, such as the density of the solid and liquid, the diameter of the solid, and not by the operation conditions. The relations between the impeller speed and the liquid velocity are different in the bottom region and the up flow wall region. The liquid velocity in the up flow wall region is not influenced by the solid concentration for just uniform suspension and the liquid velocity in just pure liquid layer are not influenced by the operational condition,etc.
出处 《北京化工大学学报(自然科学版)》 CAS CSCD 北大核心 2005年第1期33-38,共6页 Journal of Beijing University of Chemical Technology(Natural Science Edition)
基金 国家自然科学基金资助项目 (19976002)
关键词 搅拌槽 近壁区 液相速度 固体悬浮 stirred tank near wall region liquid velocity solid suspension
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参考文献3

  • 1Geisler R K, Mersmann A B, Local velocity distrbution and power dissipation rate of suspensions in stirred vessels[C], //Proceedings of the 6th European Conference on Mixing, England:BHRA, 1988, 267 - 272.
  • 2Nouri J M, Whitelaw J H. Particle velocity characteristics of dilute to moderately dense suspension flows in stirred reactors[J ]. Int J Multiphase Flow, 1992, 18:21 - 33.
  • 3包雨云,黄雄斌,施力田,王英琛.搅拌槽内固体颗粒对液相速度影响的研究[J].化学工程,2002,30(5):29-33. 被引量:9

二级参考文献6

  • 1黄雄斌,包雨云,施力田,王英琛.应用电导探针测定固-液两相流的局部速度[J].高校化学工程学报,1995,9(2):187-190. 被引量:9
  • 2Nouri J M, Whitelaw J H. Particle velocity characteristics of dilute to moderately dense suspension flows in stirred reactors[J].Int J Multiphase Flow,1992, 18:21-33.
  • 3Geisler R K, Mersmann A B. Local velocity distribution and power dissipation rate of suspensions in stirred vessels[A].Proceedings of the 6th European Conference on Mixing[C]. England:BHRA,1988.267-272.
  • 4Yianneskis M. Velocity, particle sizing and concentration measurement techniques for multiphase flow [J]. Powder Technology, 1987, 49:261-269.
  • 5Yu Z,Rasmuson A. Characterization and rotation symmetry of the impeller region in baffled agitated suspensions[A]. Proceedings of the 10th European Conference on Mixing[C]. Netherlands:ELSEVIER.2000.423-430.
  • 6Chudacek M W. Relationships between solids suspension criteria, mechanism of suspension, tank geometry, and scaleup parameters in stirred tanks[J].Int Eng Chem Fundam, 1986, 25(3):391-401.

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