Water activity-based design of a single-stage CSTR reactive crystallization process for producing super-azeotropic HCl and well grown metastable α-calcium sulfate hemihydrate crystals from CaCl2 solution

The regeneration of strong (>= 6 mol/L) hydrochloric acid (HCl) is an important but capital and energy intensive unit operation in chloride metallurgical facilities. This paper discusses a novel low temperature process capable of producing super-azeotropic hydrochloric acid via the reactive crystallization of calcium sulfate alpha-hemihydrate, a valuable by-product, in a continuous stirred-tank reactor (CSTR). The design of the process was enabled via model-based water activity calculations that allowed for selecting process conditions promoting the metastability of calcium sulfate alpha-hemihydrate in strong HCl solutions, while preventing the formation of the undesirable calcium sulfate anhydrite phase. The CSTR crystallizer was operated in the range from 13 degrees C to 60 degrees C by reacting concentrated CaCl2 feed solution (up to 5 mol/L) with concentrated H2SO4 (up to 18 mol/L). Super-azeotropic HCl (up to 9.5 mol/L, similar to 30 wt.%) and calcium sulfate alpha-hemihydrate (alpha-HH) was produced at 60 degrees C. Calcium sulfate dihydrate (DH) could also be produced but with lower strength HCl (sub-azeotropic <= 6 mol/L) and at <= 40 degrees C. By maintaining a low CaCl2 concentration (0.1-0.4 mol/L) the growth of metastable alpha-HH crystals (30-60 mu m crystal size) was promoted due to a favorable supersaturation regime. Finally, it was determined that the super-azeotropic HCl producing crystallization process can be carried out in a thermally autogenous mode at 60 degrees C taking advantage of the exothermic character of the reaction. (C) 2015 Elsevier B.V. All rights reserved.