Experiment on solid-liquid suspension in unbaffled stirred tank

被引:1
|
作者
Lai Y. [1 ]
Yang M. [1 ]
机构
[1] School of Energy and Power Engineering, Jiangsu University, Zhenjiang
关键词
Axial agitator; Eccentric agitation; Just-suspended speed; Solid-liquid suspension; Unbaffled stirred tank;
D O I
10.3969/j.issn.1671-7775.2010.03.014
中图分类号
学科分类号
摘要
Solid-liquid suspension performance in a high solid concentration was investigated. An unbaffled, flat bottom, cylindrical glass vessel of diameter d=0.34 m equaling to the liquid height was used, which was stirred with two different axial flow impellers, a ZHX propeller and a 45° pitched blade turbine(PBT) impeller. The spherical glass particles of 150 μm were chosen as dispersed phase. The particle volume fraction was 20%. The states of suspension were observed and recorded using a digital camera. The just-suspended speed was determined by making visual observations through the base of the vessel illuminated by a laser light source. The effects of impeller off-bottom clearance, type of axial impeller and eccentricity of the impeller in eccentric agitation operation on the solid suspension states, the just-suspended speed and power consumption were examined. The experimental results show that, either co-axial agitation or eccentric agitation, solid particles at the corners of the tank base can not suspend simultaneosly along circular direction. The suspension of solid particles in the stirred tank can be improved by decreasing impeller off-bottom clearance height. Solid particles reach the better suspension when using PBT than ZHX. The just-suspended speed and power consumption increase with increasing eccentricity in eccentric agitation operation. The eccentric agitation has no effective action to improve the suspension performance in a high solid concentration stirred tank.
引用
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页码:309 / 313
页数:4
相关论文
共 11 条
  • [1] Assirelli M., Bujalski W., Eaglesham A., Et al., Macroand micromixing studies in an unbaffled vessel agitated by a Rushton turbine, Chemical Engineering Science, 63, 1, pp. 35-46, (2008)
  • [2] Shan X., Yu G., Yang C., Et al., Dispersion characteristics of solid-liquid suspension in an unbaffled stirred tank, The Chinese Journal of Process Engineering, 18, 1, pp. 1-7, (2008)
  • [3] Tezura S., Kimura A., Yoshida M., Et al., Agitation requirements for complete solid suspension in an unbaffled agitated vessel with an unsteadily forward-reverse rotating impeller, Chemical Technology and Biotechnology, 82, 7, pp. 672-680, (2007)
  • [4] Karcz J., Cudak M., Szoplik J., Stirring of a liquid in a stirred tank with an eccentrically located impeller, Chemical Engineering Science, 60, 8-9, pp. 2369-2380, (2005)
  • [5] Montante G., Bakker A., Paglianti A., Et al., Effect of the shaft eccentricity on the hydrodynamics of unbaffled stirred tanks, Chemical Engineering Science, 61, 9, pp. 2807-2814, (2006)
  • [6] Cabaret F., Rivera C., Fradette L., Et al., Hydrodynamics performance of a dual shaft mixer with viscous newtonian liquids, Chemical Engineering Research and Design, 85, 5, pp. 583-590, (2007)
  • [7] Galletti C., Brunazzi E., On the main flow features and instabilities in an unbaffled vessel agitated with an eccentrically located impeller, Chemical Engineering Science, 63, pp. 4494-4505, (2008)
  • [8] Galletti C., Pintus S., Brunazzi E., Effect of shaft eccentricity and impeller blade thickness on the vortices features in an unbaffled vessel, Chemical Engineering Research and Design, 87, 4, pp. 391-400, (2009)
  • [9] Yang F., Zhou S., Zhang C., Et al., Investigation on solid-liquid suspension performance in an eccentrically stirred tank, The Chinese Journal of Process Engineering, 18, 6, pp. 1064-1068, (2008)
  • [10] Ni J., Wang G., Mechanism of hyper-concentrated flow: I. Theory, Journal of Hydraulic Engineering, 5, 5, pp. 22-26, (2000)