A model thick stock co-axial jet mixer was investigated to elucidate the im
portant factors for the dispersion of 3% consistency pulp suspensions into
a dilute white water stream. The jet breakup was characterized by simultane
ous radial sampling and by stepwise axial sampling. A combined axial and ra
dial concentration profile for the jet breakup was obtained to characterize
the mixing behaviour. The criterion for 'good mixing' was defined as the d
istance from injection where the range in radial samples was less than 5% o
f the mean. The mixing behaviour of the pulp jets differed significantly fr
om the electrolyte jet mixing. The pulp required a longer mixing zone to ac
hieve 'good mixing' with the fibre length identified as a key factor in the
dispersion. The resistance to jet dispersion exhibited by the pulp was att
ributed to the flocs present in the system and interlocked fibres promoting
jet cohesion.