Let the flow direction be , the gradient direction , and the vorticity direction , with simple shear flow and signed shear rate . Use the gradient convention established in part (a):
At steady homogeneous shear the ordinary time derivative and advection vanish. Put , and . The corotational Maxwell fluid law then gives
The equation gives , and the unforced equations force those components to zero. Solving the three displayed equations gives the steady shear of a corotational Maxwell fluid:
The deviatoric stress is indeed traceless. Its isotropic pressure contribution is irrelevant to either shear viscosity or a normal-stress difference.
Consequently the steady shear viscosity is
For , when ; it decreases with and tends to zero at large rate. This proves shear thinning directly, without confusing a decreasing viscosity with a necessarily decreasing shear stress.
With the standard definitions and ,
At zero shear both vanish; at small shear they are quadratic, consistently with part (b). The signs and the fact agree qualitatively with many polymeric-fluid experiments. However the fixed ratio often overestimates the measured second difference and cannot capture variation of that ratio with material and shear rate. For example, measurements on polyethylene show a smaller, rate-dependent relative second normal-stress difference. Thus the qualitative normal-stress signs are reasonable, but the predicted relative magnitude is not generally quantitatively satisfactory; these signs are not a universal statement about every non-Newtonian fluid.
For simple shear flow , put and . The steady deviatoric stress is
This follows by setting , in the corotational Maxwell fluid equation: , , and . Hence the shear viscosity is , which exhibits shear thinning, while and . These differences are independent of the isotropic pressure.