Let
Axial momentum balance gives shear-stress magnitude . The wall stress must exceed the pressure-dependent yield stress, so motion requires
When this holds, define the plug radius
The no-slip solid velocity is
In the sheared annulus,
so
The volume flux carried with the particle skeleton is
By Darcy law, the fluid moves relative to the solids at . The total mixture-volume flux is therefore
This is explicit because is given above. For example, if
then
At fixed , increasing increases the plug radius and lowers both the particle velocity and porosity. The total flux decreases from a nearly particle-free Poiseuille value toward a nonzero Darcy seepage flux through a jammed packing. Particles stop when , namely at
Put . As , almost the whole cross-section is a plug at concentration and speed . The particle flux is therefore
The jammed seepage flux is approximately
It appreciably changes the total flux when , or
Because , seepage matters principally in a narrow pressure interval just below jamming.
At fixed , the pressure gradient is no longer fixed. As , the constitutive law gives a dilute particle fraction and hence . Raising first adds particles and increases their flux. At high , the packing becomes dense and nearly jammed; maintaining then requires a large pressure gradient that sends most of the liquid through the packing by Darcy seepage, while falls back toward zero. Thus has an interior maximum, and every particle flux below that maximum occurs at two solid pressures.
On the low- branch the suspension is dilute, shear is distributed broadly, particle motion carries much of the total volume, and the required is relatively small. On the high- branch the suspension contains a large nearly jammed plug, particles move slowly, seepage carries a substantial fraction of , and a much larger is required. Equal particle flux therefore does not imply equal concentration, flow structure, or pumping cost.

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