The general theory of steady slow motion of non-Newtonian fluids through a tapered tube is presented in the present paper.
The general formulae for shear stress, velocity and flow have been obtained for a straight tube, a rotating coaxial cylinder viscometer, a cone and plate viscometer, and a double cone viscometer. However, no similar formula in general for non-Newtonian fluid through a tapered tube has yet been available.
It is assumed that the fluid is characterized by a time-independent flow curve f(τ), and that the tapering angle α is very small. It is further assumed that the coefficient of viscosity η which appears in the relationship between the stress and the strain rate of non-Newtonian fluid is not constant, but a function of the velocity gradient. Under these assumptions the following formulae for the shear stress, velocity, and flow have been obtained, which will be taken in general.
τa being the shear stress on the wall. These formulae, quite similar to those for a straight tube of uniform cross section, are applied to the following particular fluids: Newtonian fluid, power law fluid, Bingham body and the fluid obeying Casson's equation.