Successful bleaching of kraft pulp with hydrogen peroxide requires the
removal or deactivation of transition metals. Removal of transition m
etals with an acidic stage (with or without chelating agents) prior to
the bleach plant has proven effective in controlling transition metal
s when the acidic stage washer filtrate is sewered. However, if the bl
each plant is closed by bringing the acid stage filtrate back as showe
r water to the brown stock washers, a portion of the metals can be red
eposited onto the pulp. Under certain conditions, this recycle of meta
ls results in a net increase of transition metals to the bleach plant.
In addition, the concentration of scale-inducing metals can increase
throughout the fibreline and in the weak black liquor. A mathematical
model based on ion exchange and chelation theory has been developed to
represent the binding of metals to kraft pulp. The model predicts the
distribution of Na, Ca, Mg and Mn over a broad range of pHs, metal co
ncentrations and chelating agent concentrations. The model has been va
lidated with a series of laboratory experiments investigating the remo
val of the metals from kraft pulp by chelation pretreatment and acid w
ashing.