The carbon-in-pulp (CIP) process is used extensively in the mining industry
to recover dissolved gold from cyanide-leached pulps. The pulp normally co
ntains inorganic material that could penetrate the pores of the carbon. In
the formulation of the model it was proposed that the loading of solid spec
ies from the hulk suspension onto activated carbon is dependent on differen
t probabilities such as the activity of pores at the outer shell of the car
bon, the concentration of fines in suspension, the stirring speed of the su
spension, zeta potential of solid fines, and the fraction of fines smaller
than the size of a specific pore.
The proposed model was shown to describe the intrusion of solid fines in ca
rbon accurately under a wide variety of conditions. The model was not so se
nsitive towards zeta potential of the solid particles or the effective stir
ring speed. The concentration of solid fines in the suspension influenced t
he collision-kinetics and hence the rate of intrusion. The concentration de
cay of solid fines in suspension was very sensitive at low concentrations,
whereas at high concentrations the model-output concentration remained cons
tant.