“…The experimental results are predicted by using an associated-solution model [1] having binary parameters obtained from binary phase equilibria and are reproduced by modified and extended forms of the UNIQUAC models [2,3] including ternary and quaternary parameters obtained from the ternary and quaternary (liquid + liquid) equilibria in addition to binary ones. The binary (vapour + liquid) equilibria, mutual solubility and ternary (liquid + liquid) equilibria relevant to the quaternaries have been available from the literatures: (vapour + liquid) equilibria, (methanol + TAME) [4], (methanol + MTBE) [4], (methanol + toluene) [5], (TAME + MTBE) [6], (TAME + toluene) [7], (MTBE + toluene) [8], 0021 (TMP + toluene) [9], (TAME + TMP) [7] and (MTBE + TMP) [10]; mutual solubilities, (methanol + TMP) [1]; ternary (liquid + liquid) equilibria, (methanol + TA-ME + TMP) [1], (methanol + MTBE + TMP) [1] and (methanol + toluene + TMP) [1].…”