Turbulent flow of non-Newtonian substances |
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Authors: | J. J. Vocadlo P. J. Wheatley M. E. Charles |
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Affiliation: | (1) Worthington (Canada) Ltd., Brantford, Ontario, Canada;(2) Dept. of Chem. Engineering and Applied Chemistry, University of Toronto, M5S 1A4 Toronto, Canada |
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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 factorm 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 - t exponent defined by eq. [1] - V mean velocity - V* volume of particles in pipe lengthL - W settling velocity of particles - m factor defined by eq. [1] - shear rate - turbulent pseudo shear rate defined by eqs. [8] and [9] - w wall shear stress - (w)s increment in wall shear stress due to presence of settling particles - µm limiting viscosity at high rate of shear - 1 density of carrier liquid - m density of mixture - s density of solidProfessor of Chemical Engineering, University of Toronto and scientific advisor to Worthington (Canada) Ltd.With 8 figures |
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