A dynamic model of a countercurrent brownstock washing system was buil
t in order to develop and evaluate process control strategies. For a s
ingle industrial stage, approximately 90 minutes were required to achi
eve 95% of a new steady state following a step-change in the dissolved
solids concentration in the feed stream. Response times became very l
arge for several washers in series. When the dilution factor was manip
ulated, about 75% of the change in the dissolved solids concentration
in a washed pulp stream occurred instantaneously.