The crystallization of phenanthrene from toluene with carbon dioxide a
s the antisolvent gas is described. In the GAS process, a pressurized
gas is dissolved into a liquid solvent, where it causes a volumetric e
xpansion and lowers the solubility of the solute. Theoretical models a
ve presented for the liquid-phase expansion and the solubility as a fu
nction of pressure and temperature. The Nyvlt theory for batch crystal
lization is adapted to predict the pressure profile in the crystallize
r needed to maintain a constant supersaturation and growth rate. Gener
ation of seeds is accomplished via a pressure pulse at the saturation
pressure. The average particle size of the phenanthrene could be varie
d from 160 to 540 mu m. Creation of seeds doubles the particle size an
d reduces the coefficient of variation significantly. The residual amo
unt of toluene in the crystals without treatment is approximately 70 p
pm. The particles are agglomerates of phenanthrene crystals.