Studies on the chlorination of a sphalerite concentrate in aqueous slurry b
y gaseous chlorine have been carried out. The effect of time, flow rate of
Cl-2, partial pressure of Cl-2 in N-2 (p(Cl2)), particle size and pulp dens
ity of the sulphide concentrate and the temperature of chlorination, on the
fraction of the zinc dissolved, has been investigated. At the optimum flow
rate of Cl-2 (350 ml min(-1)), the percent of Zn dissolved is found to be
increasing with decrease in particle size and pulp density, proportional to
p(Cl2) (0.2 to 1.0 atm) and increases with increase in temperature in the
range of 10 to 28 degrees C, studied. The activation energy of the chlorina
tion process has been calculated to be 49.6 kJ mol(-1). In all the cases, t
he fraction of the Zn dissolved (a) in time (t) is found to follow a diffus
ion reaction control model: 1 - 2/3a - (1 - a)(2/3) = kt, where k is the ra
te constant. At 28 degrees C, with 12 wt.% concentrate in the slurry acid u
sing pure Cl-2 gas with a flow rate of 350 ml min(-1), nearly 90% of Zn ext
raction has been achieved in about 17 min. (C) 1999 Published by Elsevier S
cience B.V. All rights reserved.