An industrially feasible process was proposed to produce α-calcium sulfate hemihydrate (α-HH) from FGD gypsum without any additives. In this process, an AlCl 3 solution was used to promote the conversion of calcium sulfate dihydrate (DH) to hexagonal prismatic α-HH with high strength at atmospheric pressure. The phase transition kinetics of FGD gypsum was experimentally investigated under conditions: AlCl 3 (2−2.5 m), MgCl 2 (0−0.4 m) existing in raw FGD gypsum, and the solid−liquid ratio (or solid content %) range of 0.1−2 at 363 K. It was found that increasing the concentrations of MgCl 2 in AlCl 3 solution accelerated the conversion. The uniform large hexagonal prism HH product was obtained at the folowing optimal conditions: 2.5 mol/kg AlCl 3 , 0.4 mol/kg MgCl 2 , solid−liquid ratio of 2, and equilibration time of 2 h at 363 K. The phase diagram of the AlCl 3 -MgCl 2 -H 2 O system was determined by measuring solubility of solids. The E-NRTL activity model was used to construct the phase transition diagram of CaSO 4 in AlCl 3 −MgCl 2 media and to judge the stable range of DH and HH.