A set of empirical temperature-molar fraction expressions for solid-liquid equilibrium curves of LiBr-H2O and LiCl-H2O systems is presented. The expressions are based upon a body of experimental data that have been compiled and critically evaluated. The equations cover the full composition range for LiCl-H2O system and compositions up to the salt mole fraction of x = 0.46 (i.e. mass fraction of w = 0.805) for LiBr-H2O, corresponding to transition from monohydrate to anhydrate. Temperatures and solution compositions at the eutectic point and at transition points between hydrates have been determined from intersections of the curves corresponding to the adjacent hydrate ranges of the phase diagram. Equations of a special structure were used, involving the coordinates of the transition points as parameters, which makes possible their direct non-linear optimization. To obtain more reliable results, a procedure was employed optimizing both the temperature-composition and composition-temperature equations simultaneously. The uncertainty in the obtained values of the transition point coordinates are estimated to be of the order of I K for temperature and 0.001 for the composition expressed in salt mole fraction. Gaps in the database are shown to give experimenters orientation for future research. (c) 2006 Elsevier B.V. All rights reserved.