Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

ABSTRACT

The solubility for the aqueous ternary system (NH4)2SO4 + Na2SO4 + H2O at T = (303.15 and 313.15) K and p = 0.1 MPa were investigated experimentally with the method of isothermal dissolution equilibrium. In the phase diagram of the ternary system at 303.15 K, there is eight crystallization regions, four univariant curves, and three invariant points corresponding to (Na2SO4*10H2O + Na2SO4), (Na2SO4 + Na2SO4*(NH4)2SO4*4H2O) and (Na2SO4*(NH4)2SO4*4H2O + (NH4)2SO4). However, in the phase diagram of the same ternary system at 313.15 K, the crystallization region of Na2SO4*10H2O is disappeared, and there are three single salt crystallization regions corresponding to Na2SO4, Na2SO4*(NH4)2SO4*4H2O and (NH4)2SO4. A comparison of the phase diagrams for this ternary system at (273.15, 288.15, 298.15 K, 303.15, 313.15 and 333.15) K shows that the area of Na2SO4*(NH4)2SO4*4H2O and (NH4)2SO4 is increased obviously whereas the area of Na2SO4 (or Na2SO4*10H2O) is decreased significantly and no solid solution was found. The experimental phase equilibria and phase diagrams can provide fundamental basis for salt recovery in industrial wastewaters.