Pressure screens are the most efficient and practical unit operation for fi
bre length separation. Screens are used individually and in systems. It is
not a simple task to decide which configuration to use, and what screen pla
te, reject rate and dilution water flow rate are most appropriate in each s
tage. Rules exist for designing systems for contaminant removal, however it
is not known how well-suited these are for fractionation. The objective of
this work was to propose a model and approach to optimize screening system
s for fibre length fractionation. Optimization was used to compare the perf
ormance of a single-stage and four two-stage systems. Limits on the maximum
reject consistency, maximum total dilution and minimum aperture size were
used to constrain the solutions to practical values. The proposed methodolo
gy is potentially useful for fine-tuning existing screening systems, and fo
r testing novel process designs.