In the second part of this two-part study, molecular dynamics simulati
ons are performed for a fluid of spherical molecule in Couette flow. T
he simulation uses the same system as that in Part 1, but with the top
wall translating in the x direction to generate a Couette flow. The s
hear equivalent viscosity eta(es) of a fluid is found to increase as f
ilm thickness decreases. The dependence is similar to that of the flow
equivalent viscosity eta(ef) obtained in Part 1, but the shear viscos
ity eta(cs) exhibits a smaller value and slower increase rate. A furth
er comparison between eta(es) and eta(ef) shows that at the him thickn
ess where the viscosity eta(ef) diverges, the corresponding shear visc
osity keeps a relatively small value, which is attributed to the large
r shear rate applied in simulation of Couette flow. In a region where
shear rate is low, the shear viscosity remains almost constant until a
critical shear rate gamma(c) is reached, then the 'shear-thinning' fo
llows, i.e, the viscosity declines in a power-law, eta(es) similar to
gamma(-2/3), and the mean shear stress approaches a constant value-the
'limiting shear stress'. If the film becomes molecularly thin, the lu
bricant behaves like a viscoelastic material, indicated by the conside
rable value of shear stress existing at the zero shear rate. The mean
velocity profile of molecular flow shows a linear distribution, but wi
th inflexions on the profile near the wall-fluid interface. When a ver
y high shear rate is applied, however, the flow in thin films seems to
be divided into two parts, half stays almost at rest and half is rapi
dly sheared. Once the stress exceeds the limiting shear stress, a slip
in velocity appears at the solid-fluid interface.