The flow of polymeric liquids in a porous medium of variable permeability r
epresented by a cylindrical tube randomly packed with glass spheres is stud
ied. The cylinder represents two porous media of different permeabilities a
nd same porosity arranged in series. We show that the energy loss is higher
if the polymeric solution flows first through the porous medium with the s
maller permeability rather than through the section of the cylinder with th
e larger permeability. The difference in energy requirements increases with
increasing Reynolds number and may be as high as 25-35 percent for Reynold
s numbers of O(I). This is a novel effect not observed for Newtonian and hi
ghly shear thinning inelastic fluids flowing through the same configuration
. Energy requirements for the same volume flow rate are much higher than a
Newtonian fluid of the same zero shear viscosity as the polymeric solution.
Energy loss increases with increasing Reynolds number at a fixed concentra
tion to level off at a Reynolds number of O(I). At a fixed Reynolds number,
the loss is a strong function of the concentration and shows large increas
es with increasing concentration. For shear-thinning oil field spacer fluid
s De similar to 0.1 represents a good criterion for the onset of elasticity
effects. For solutions of polyacrylamide De similar to 0.1 corresponds app
roximately to the flow rate at which pressure drop starts becoming dependen
t on the flow direction. Expressions for the friction factor and the resist
ance coefficient as a function of the Reynolds number have been developed u
sing the inelastic KPK (Kutateladze-Popov-Kapakhpasheva) and viscoelastic e
ight constant Oldroyd models, respectively. The behavior of inelastic shear
-thinning and viscoelastic fluids as represented by oil field spacer fluids
and aqueous solutions of polyacrylamide is predicted qualitatively except
the difference in energy requirements when the flow direction is reversed i
n the case of the latter.