A Bingham plastic is a yield-stress fluid, and hence a non-Newtonian fluid. It is also an instantaneous generalized-Newtonian model after yielding. It cannot describe memory-dependent viscoelasticity, including stress relaxation, elastic recoil, and time-dependent normal-stress effects.
For scalar shear stress and shear rate , its complete ideal constitutive law is
Equivalently, in yielded material,
Set , so . For the unidirectional velocity , the axial inertialess Cauchy momentum equation is
The free surface is shear-free, , and integration gives
This result follows from force balance alone, so it is independent of the constitutive equation and of .
The axial shear force exerted by the liquid on the cylindrical fibre is therefore
Its direction is downstream; the reaction on the fluid is upstream. In particular, the yield stress changes the velocity field but not the total force required by the imposed pressure drop.
The shear stress decreases monotonically from the fibre to zero at the free surface, so its maximum is
Flow occurs precisely when this exceeds the yield stress:
When this condition holds, there is one yield surface determined by
The region is yielded and the outer region is an unyielded plug flow of a yield-stress fluid. In the yielded region, . The no-slip condition gives
The unyielded layer translates without shearing at the plug speed
The local motion is simple shear with flow direction , gradient direction , and vorticity direction . Writing , a second-order fluid has first and second normal-stress differences
Up to an isotropic contribution absorbed into pressure, a convenient representation is
Thus both the flow-direction and gradient-direction normal stresses can be nonzero, while the radial momentum equation becomes
The first normal-stress coefficient affects but cancels from radial balance.
In the yielded layer,
Moreover,
Consequently has the sign opposite to and is independent of . For the common case , pressure increases radially outward toward the free surface.

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