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Turbulent flow of non-Newtonian substances
Authors:J. J. Vocadlo  P. J. Wheatley  M. E. Charles
Affiliation:(1) Worthington (Canada) Ltd., Brantford, Ontario, Canada;(2) Dept. of Chem. Engineering and Applied Chemistry, University of Toronto, M5S 1A4 Toronto, Canada
Abstract:Summary A unique shear stress-shear rate relationship exists for laminar flow of any time independent substance in a tube, whereas this is not the case for turbulent flow. In order to obtain a unique relationship for turbulent flow, a new approach based on the elementary theoretical interpretation of experimental data is adopted in the present paper. In particular, wall shear stress is found to be a unique function of a new turbulent pseudo shear rate term. In this relationship therè are two parameters which characterize a given substance — the limiting viscosity at high shear rateµm and a factoragrm which takes into account modification of turbulent structure by the non-Newtonian properties. Both of these parameters must be determined experimentally. Methods of predicting pressure gradients and of scaling up are outlined. In applying the approach to suspensions in which the solid phase has a density greater than that of the liquid medium, it may be important to determine the increment in shear stress equivalent to the energy required to maintain the solid particles in suspension.The validity of this approach is confirmed by data for the flow of a variety of substances including kaolin suspensions and Carbopol solutions in tubes ranging in diameter from 1.5 to 20 mm.Nomenclature C volume fraction solid in suspension - D tube diameter - f Darcy-Weisbach friction factor - g gravitational acceleration - Ks proportionality constant defined by eq. [10] - L length of tube - P pressure - Re Reynolds number
$$frac{{rho _m VD}}{{mu _m }}$$
- t exponent defined by eq. [1] - V mean velocity - V* volume of particles in pipe lengthL - W settling velocity of particles - agrm factor defined by eq. [1] - 
$$dot gamma $$
shear rate - 
$$dot gamma _{turb.} $$
turbulent pseudo shear rate defined by eqs. [8] and [9] - tauw wall shear stress - (tauw)s increment in wall shear stress due to presence of settling particles - µm limiting viscosity at high rate of shear - rgr1 density of carrier liquid - rgrm density of mixture - rgrs density of solidProfessor of Chemical Engineering, University of Toronto and scientific advisor to Worthington (Canada) Ltd.With 8 figures
Keywords:
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