The kinetics of desilication of synthetic, sodium aluminosilicate solution
(spent Bayer liquor) and growth of sodalite crystals have been studied unde
r isothermal, batch crystallization conditions dose to those prevailing in
Bayer process heat exchangers. The desilication rate of the liquor via the
formation and growth of sodalite scale on steel substrates was found to be
independent of agitation rate. With sodalite seeding, the desilication rate
was observed to increase dramatically due to seed crystal growth with the
suppression of scale formation. An activation energy of 30 kJ mol(-1) and a
second order dependence of the desilication rate on relative supersaturati
on of SiO2 were obtained for sodalite crystal growth. (C) 1999 Elsevier Sci
ence B.V. All rights reserved.