This paper describes numerical solutions for the laminar flow of non-N
ewtonian fluids in vertical annuli using the Herschel-Bulkley model to
describe the rheological behaviour of such materials. Numerical solut
ions have been obtained when there is both axial and tangential flows
in either a concentric or eccentric annulus. The tangential flow arise
s from the rotation of the inner cylinder of the annulus and the axial
flow from a constant axial pressure gradient. The flow is analysed by
solving the momentum and continuity equation numerically using the fi
nite element method. The dimensionless velocity, deformation and stres
s profiles with other quantities such as the apparent viscosity and pr
essure distribution have been calculated for various eccentricities, r
adius ratios, fluid properties and flow parameters; the results give i
nsights into the flow behaviour in the annuli. It is shown that the in
clusion of rotational effects, for a fixed pressure gradient, is likel
y to increase the axial volumetric flowrate over non-rotating situatio
ns in concentric geometries. New results reveal that, in eccentric ann
uli, the situation is reversed and the flowrate gradually decreases as
the rotation rate is increased.