The microcline-CaSO4-CaO system was determined to be used to obtain K2
SO4 by thermodynamical analysing and computing lots of possible reacti
ons of 6 microcline :systems. The effects of roasting temperature, tim
e and ratios;of reactants on the potassium recovery of the microcline-
CaSO4-CaCO3 were studied and the favorable conditions were determined
as follow: 1323 K, 3.0 h, m(microcline) : m (CaSO4 . 2H(2)O) : m (CaCO
3) = 1 : 1 : 3. In the presence of 0.9% additive I, the roasting tempe
rature decreased from 1323 K to 1223 K and the potassium recovery was
84%. Kinetic experimental data of the two systems with or without addi
tive I both fitted a diffusion-through-product-layer-reaction model, a
nd their kinetic equations were presented with apparent activation ene
rgies 184.4 kJ . mol(-1) and 158.9 kJ mol(-1) respectively.