期刊文献+

螺带桨叶在粘弹性流体中的搅拌功率 被引量:4

Power Consumption for Agitating Viscoelastic Liquids with Helical Ribbon Impellers
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摘要 本文研究了层流区内外单螺带-锚、四螺带-锚桨叶在粘弹性流体中的搅拌功率消耗。与牛顿型流体比较结果表明,流体的弹性对搅拌功率有较大的影响。Boger流体较牛顿型流体的功率消耗大50%以上。本文采用了广义二阶流体本构方程导出搅拌功率计算式:NpReafs^(1-n)=Kpfvfs^2[1+F^*1avfa(m-n-3)Wi/Ks^2]用实验数据确定fs和F^1av,得到了适用于牛顿型流体、假塑性流体和粘弹性流体的功率计算式。计算结果与实验值比较接近。 The power consumption for agitating viscoelastic fluids including Boger fluids and Newtonian fluids in the laminar regime were compared for the inner-and-outer helical ribbon-anchor and the four helical ribbon-anchor impellers. The influence of elasticity on power consumption is significant. For Boger fluids the power consumption could be up to 1.5 times of that fro Newtonian fluids.The power consumption correlations:for agitating Newtonian, pseudoplastic and viscoelastic fluids was developed by means of a second-order elastic fluid rheological model. The parameters f_v,f_s and F~*_(1av) were determined experimentally. The predicted results agree with experimental data.
机构地区 浙江大学化工系
出处 《化工学报》 EI CAS CSCD 北大核心 1989年第5期626-634,共9页 CIESC Journal
基金 自然科学基金资助项目
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参考文献3

  • 1朱秀林,化学工程,1985年,1期,52页
  • 2匿名著者,聚合物加工流变学,1985年
  • 3陈文芳,非牛顿流体力学,1984年

同被引文献34

  • 1王凯,朱秀林,潘祖仁.内外单螺带—锚搅拌槽中粘弹性流体的流速分布和混合时间[J].浙江大学学报(自然科学版),1989,23(1):39-48. 被引量:2
  • 2陈克复,颜进华,杨光誉.对压力筛筛选机理及效率评定方法的新认识[J].中国造纸,1996,15(6):51-55. 被引量:4
  • 3永进治.混合原理与应用[M].化工出版社,1984..
  • 4Coulson J M, Richardson J F, et al. Chemical Engineering [M]. Oxford: Pergamon Press, 1990.
  • 5Bakker A, Gates L E. Properly choose mechanical agitators for viscous liquids[J]. Chem Eng Progress, 1995, 91: 23- 34.
  • 6Delaplace G, Torrez C, Leuliet J C, et al. Experimental and CFD simulation of heat transfer to highly viscous fluids in an agitated vessel equipped with a non standard helical ribbon impeller[J]. Tans IChemE, 2001, 79(Part A):927-937.
  • 7Chhabra R P. Fluid mechanics and heat transfer with non- Newtonian liquids in mechanically agitated vessels [ J ]. Advances in Heat Transfer, 2003, 37:77-178.
  • 8Paul E L, Atiemo-Obeng V A, Kresta S M. Handbook of Industrial Mixing[M]. New York: Wiley, 2004.
  • 9Jean-Philippe Torre, David F Fletcherb, Thierry Lasuyec, et al. Single and multiphase CFD approaches for modelling partially baffled stirred vessels: Comparison of experimental data with numerical predictions [ J]. Chemical Engineering Science, 2007, 62: 6246-6262.
  • 10Hristov Hristo Vesselinov, Boden Stephan, Hampel Uwe, et al. A study on the two phase flow in a stirred tank reactor agitated by a gas-inducing turbine[J]. Chemical Engineering Research and Design, 2008, 86:75-81.

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