SCOPEA good deal is known about gas-liquid equilibria of paraffin mixtures, and the location of the gas-liquid critical lines (critical locus) has been determined for many binary mixtures of this type (Kay, 1968). Little information, on the other hand, is available on their thermodynamic properties in the supercritical phase. Some of these properties, for example the negative partial molar volumes of mixtures containing polar components (Ehrlich and Fariss, 1969) and presumed to exist in binary paraffin mixtures with components of sufficient size difference as well, appear quite anomalous in the context of the behavior of liquid mixtures at low reduced temperatures. The paraffin pair chosen represents two components of a most important homologous series which differ substantially in chain length. Any generalization of the results obtained in a study of the system ethane-n-heptane to mixtures in which the components exhibit varying molecular sizes and size differences is likely to be of interest in petroleum recovery and refining, as well as in the engineering of high pressure polyethylene processes. (The mixture ethane-polymethylene is a good model for ethylene-polyethylene.) Since, according to transition state theory, the pressure-coefficient of the reaction rate constant can be represented in terms of the compressibility of the mixture and the partial molar volumes of reactants and activated complex, a knowledge of the volumetric properties of supercritical systems should help in a solution of kinetic as well as thermodynamic problems.Molar volumes of the mixture ethane-n-heptane were therefore measured in the supercritical region, including the vicinity of the critical locus, over a pressure, temperature, and composition range corresponding to nearly pure ethane to about 20 mole #Yo heptane, and partial molar volumes were obtained by the analysis of volume-composition plots constructed from pressure-volume isotherms. The results were compared with two different sets of calculations based on equations of state.
CONCLUSIONS AND SIGNIFICANCETwo approaches were found which were, in general, qualitatively successful in predicting the molar volumes and partial molar volumes in the region investigated. One of these was based on the reduced equation of state of Flory, Orwoll, and Vrij (FOV), used in conjunction with Prigogine's principle of corresponding states (PPCS) for chain molecule mixtures, the other on the Redlich-Kwong (RK) equation of state. The former method, in its original form, involves fewer arbitrary assumptions and can be extended in a straightforward manner to other binary mixtures of the same homologous series. The FOV equation was, however, proposed for liquids (negligible reduced pressure and low reduced temperature), and an empirical adjustment of its parameters was required for a good fit of the experimental data. The RK equation, on