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Flow of a simple non-newtonian fluid past a sphere
Authors:John Slattery
Affiliation:(1) Department of Chemical Engineering, Northwestern University, Evanston, Illinois, U.S.A
Abstract:Summary Creeping flow past a sphere is solved for a limiting case of fluid behaviour: an abrupt change in viscosity.List of Symbols dij Component of rate-of-deformation tensor - Fd Drag force exerted on sphere by fluid - Gtau(d) Coefficients in expression for tauij in terms of dij - GYOJKtau(d) Coefficients in power series representing Gtau(d) - R Radius of sphere - r Spherical coordinate - V Velocity of fluid very far from sphere - vi Component of the velocity vector - x Dimensionless radial distance, r/R - xi Rectangular Cartesian coordinate - beta Dimensionless quantity defined by (26) - Gcytau(d) Potential defined by (7) - gamma Value of x denoting border between Regions 1 and 2 as a function of theta - eegr1, eegr2 Lower and upper limiting viscosities defined by (10) - theta Spherical coordinate - theta* Value of theta for which gamma=1 - 
$$tilde theta $$
Value of theta denoting border between regions 1 and 2 as a function of x - mgr Newtonian viscosity - tauij Component of the stress tensor - phiv Spherical coordinate - psgr1, psgr2 Stream functions defined by (12) and (14) - 
$$begin{gathered}bar Ibar I_{d,} bar Ibar I_tau  , hfill bar Ibar Ibar I_{d,} bar Ibar Ibar I_tau   hfill end{gathered} $$
Second and third invariants of the stress tensor and of the rate-of-deformation tensor, defined by (3)
Keywords:
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