Chloride and potassium are two problematic minor components which can
accumulate in kraft pulping chemical recovery cycles. There is an enri
chment of these two elements in recovery boiler electrostatic precipit
ator dust and so this is a good point from which to remove them. The m
ass flow rate of the electrostatic precipitator dust has been quantifi
ed in two field studies, and the effect of four different boiler opera
ting parameters on this mass flow rate has been evaluated. The results
show that the recycle dust varies between 3.5 to 10% of the as-fired
black liquor solids content. A process for selectively removing chlori
de and potassium from electrostatic precipitator dust has been develop
ed.