In non-monotonic flow, the graph of flow rate versus shear stress or pressure often forms an S-shaped curve. Initially, the flow rate increases with stress. At a certain threshold, further increases in stress cause the flow rate to drop. fluid can exhibit two different shear rates at the same shear stress, causing a separation or banding in shear rates.
In vorticity banding different regions have distinct shear stresses but the same shear rate.
Weienberg-Rabinowitsch allows for calculating the shear rate at the tube wall, even when a fluid’s viscosity changes with shear rate.
Wyart and Cates rheological model is used in this study. It explains the behavior of shear-thickening fluids—specifically, how their viscosity increases abruptly under certain conditions.
ηr is the viscosity when all contacts are frictional, ns is for frictionless contacts. Q is flowrate, delta P is pressure drop
At low concentrations the curve is smooth and almost linear, indicate a continuous shear-thickening (CST) behavior. As concentration increases fluid exhibits discontinuous shear thickening (DST), where viscosity increases abruptly. At very high concentrations the curve forms an S-shape, indicating non-monotonic behavior. Here, the shear rate can decrease with increased shear stress, leading to instabilities like shear banding.
When this type of fluid flows in a tube, streamwise banding occurs, here the pressure gradient can be inhomogeneous, dividing into regions of high viscosity and low viscosity along the tube.
In study, experiment was done at homogeneous and heterogeneous initial conditions. Initially, the flow rate is high. The dispersion of the pressure gradient is a result of the initial distribution of friction and viscosity. With time, the flow rate decreases and the different pressure gradients diverge. Some locations converge to a low gradient, while others converge to a higher pressure gradient.
source:
https://universite-paris-saclay.hal.science/hal-04743748