Abstract
Isothermal, batch desilication kinetics of synthetic, sodium aluminate solution (spent Bayer liquor) via cancrinite and cancrinite/sodalite mixed-phase crystal growth, have been studied under conditions at which sodium aluminosilicate scale forms at the surfaces of steel heat exchangers of alumina plant. Seeding with the pure cancrinite and mixed-phase crystals results in the suppression of scale formation and a faster rate of liquor desilication in comparison with its sodalite dimorph. Cancrinite seed crystals prepared from NO − 3-rich solutions exhibited crystal growth mechanism and kinetic behaviour different from dimorphic mixed-phase crystals prepared from CO 2− 3-rich solutions, when both were used to desilicate CO 2− 3-rich spent Bayer liquor. The rate of desilication due to crystal growth on CO 2− 3-cancrinite/sodalite mixed phase crystals followed a second-order dependence on the relative supersaturation of SiO 2. An activation energy of 52 kJ mol −1 was estimated for the crystal growth process. For desilication kinetics involving NO − 3-cancrinite seed crystal growth, a third-order dependence on relative supersaturation of SiO 2 and an activation energy of 63 kJ mol −1 were obtained.
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