Fibre fractionation and selective processing of each fraction produces high
er quality, more uniform pulp. Engineering efficient pressure screening sys
tems requires appropriate performance equations. This study extends previou
s screening performance equations by comparing pilot screening trials with
a mechanistic model of fibre passage through the screen to predict the effe
cts of reject rate, slot width, contour type, and slot velocity on fraction
ation and consistency changes. Smooth-hole screen plates were found to frac
tionate more efficiently than contour-slot screen plates. Fibre passage thr
ough slotted screen plates was strongly dependent on the fluid velocity pas
sing through the slot, while smooth-hole apertures were approximately indep
endent of aperture fluid velocity. The maximum fractionation efficiency for
slotted plates occurred at slot velocities between 0.5 and 1.0 m/s. The na
ximum fractionation efficiency for both slot and hole plates occurs at a re
ject ratio that results in a reject thickening factor greater than two.