An isotropic simple fluid has local stress determined by the deformation history of the material element. A viscometric flow is one whose relative deformation history is that of steady simple shear flow, up to rigid changes of frame. At a given element the shear rate is constant along its history, although it can differ between elements. This includes the locally simple-shear kinematics used in standard viscometric measurements.
Use the component-first velocity gradient . The first two Rivlin-Ericksen tensors are
In the axes of a steady shear , the relative deformation gradient over a lag is , since . The material history is determined by , and its tensor symmetries exclude and stress components. The remaining symmetric stress consists of an isotropic part, one shear component, and two independent normal-stress differences. The relevant matrices are
Thus span the allowed stress components. Material isotropy and reversal of the shear show that their scalar coefficients depend on . Define the viscometric functions by
Solving for the matrix coefficients gives
This is an exact steady-viscometric representation, rather than an assumption that the fluid is everywhere a second-order fluid. The shear viscosity measures the shear resistance, while and measure the first and second normal-stress differences generated by shear. Their zero-rate values are understood as limits when these exist. An isotropic pressure changes neither normal difference.
For a flow in the lubrication approximation with gap , longitudinal scale and speed , the shear-rate scale is . The viscous shear force per unit volume scales as . Quadratic viscoelastic normal stresses scale as ; their longitudinal gradients, and the comparable mixed-component corrections, contribute forces of scale . Therefore the normal-stress smallness in lubrication criterion is
Equivalently, the thin-gap aspect ratio must multiply the shear-based elastic parameter to give a small quantity: . Normal stresses need not themselves be smaller than the shear stress; it is their effect on the leading force balance that matters. If the flow changes on an additional short time scale , the term also requires for its neglect. Material coefficients should be evaluated at the characteristic shear rate.
Now take positive cylinder rotation, measure counterclockwise from the rightward horizontal, and let increase outward through the film. The tangent has upward component , so the tangential gravitational acceleration is . To leading order in , neglect inertia and higher-order hydrostatic or capillary pressure gradients, and write . Tangential force balance and the shear-free free surface give
hence
The wall shear stress is . It opposes rotation on the uphill side and assists it on the downhill side.
For a power-law fluid, . Its inversion must retain the sign:
Integrating with the no-slip boundary condition yields
The volume flux per unit axial length is . The integrated bracket is , so the power-law coating on a rotating cylinder has
At the gravitational term vanishes by continuity. Steady mass conservation makes independent of .
On the uphill half, put and . The local flux is , with
It has a unique maximum at
A positive coating must carry the same steady flux at every angle. The tightest local bound occurs at , not on the downhill side, where the flux increases monotonically with thickness. Consequently
For the thinner positive root on the uphill side connects through to the unique downhill root, giving a periodic leading-order coating profile. At the limiting flux the two uphill roots meet at ; it is the maximum flux of this lubrication model, with a possible limiting corner resolved by neglected higher-order effects. For the check is . All these conclusions require the resulting film to remain thin enough for the lubrication approximation and for the neglected normal stresses and inertia to satisfy their scaling restrictions.