Excess enthalpies provide quantitative information about the temperature dependence of the excess Gibbs energy G(E). This information should therefore be used together with other results (vapor-liquid equilibria, liquid-liquid equilibria, limiting activity coefficients, and azeotropic data) for fitting simultaneously temperature-dependent G(E) model parameters or interaction parameters of group contribution methods. Although a large number of H(E) measurements have been published, results at temperatures other than 298.15 K are scarce. In this paper a flow calorimeter is described, and excess enthalpy data are given for the test systems n-hexane + cyclohexane, benzene + cyclohexane, and methanol + water at 298.15 K as well as for 1,1,1-trichloroethane + n-pentane, + n-heptane, + acetone, + 2-butanone, + methyl acetate, and + ethyl acetate at 363.15 K. The results were used for the systematic development of the group contribution method (modified UNIFAC) developed at Dortmund.