LetAxial momentum balance gives shear-stress magnitude . The wall stress must exceed the pressure-dependent yield stress, so motion requiresWhen this holds, define the plug radiusThe no-slip solid velocity isIn the sheared annulus,so
The volume flux carried with the particle skeleton isBy Darcy law, the fluid moves relative to the solids at . The total mixture-volume flux is thereforeThis is explicit because is given above. For example, ifthen
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 thereforeThe jammed seepage flux is approximatelyIt appreciably changes the total flux when , orBecause , 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.
Articles by others on the same topic
There are currently no matching articles.