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