A solvent is one key component in a chemical transformation. As a reaction medium it
controls the interactions between reaction partners through heat transfer and intermolecular …

Generally, molecular thermodynamic models for treating the phase equilibria of solutions
can be classified into two categories: activity coefficient relations and equations of state. The …

Experimental densities for the compressed liquid phase are reported for dimethyl carbonate
and octane, and nine of their mixtures over the composition range (0.1≤ x≤ 0.9), the …

A reliable equation for the excess heat capacity CVE at constant volume is derived from
Guggenheim's quasi-chemical lattice theory of liquid mixtures for the case of equal-sized …

Systems of N, N di (n-alkylamides)(hereafter, N, N-dialkylamides) with alkane, benzene,
toluene, 1-alkanol or 1-alkyne have been investigated in the framework of the DISQUAC …

Binary mixtures of alkoxyethanols, CH3–(CH2) n–O–(CH2CH2O) mOH, and n-alkanes or
cyclohexane are characterized in terms of DISQUAC. The corresponding dispersive (DIS) …

Étude de mélanges binaires d'aniline en présence de benzène, de toluène, d'alcane,
d'alcanol et de N, N-dialkylamide dans le contexte du modèle DISQUAC. Les paramètres …

Equilibrium temperatures for liquid–liquid and solid–liquid transitions of systems containing
sulfolane and propan-1-ol, butan-1-ol, octan-1-ol or tetradecan-1-ol were measured by a …

Thermodynamic properties, vapor–liquid equilibria (VLE), molar excess Gibbs energies
(GE), molar excess enthalpies (HE) and natural logarithms of activity coefficients at infinite …

The design of separation processes is based on the solution of the equations for material
and enthalpy balances. For this, a reliable knowledge of the real behaviour of …