Based on theoretical analysis, a continuous vertical settler was found capa
ble of fractionating fibres according to their length. Fractionation experi
ments confirm the theoretical predictions. Under the extreme dilution used
in this study, there was no effect of feed consistency. The performance of
fibre fractionation decreased with an increase in the overflow stream flow
rate. Fibre fractionation performance improved for a larger fibre diameter.
A theoretical model was developed to simulate fractionation in the continu
ous vertical settler and it agrees fairly well with the experimental result
s.