where R is the gas constant, which is 8.314 J·mol −1 ·K −1; p, v and T are pressure (Pa), molar volume (m 3 ·mol −1) and temperature (K), respectively; a is the energy parameter, b is the volume parameter; T c, p c and ω are the critical temperature (K), critical pressure (Pa) and acentric factors of the pure material, respectively.Dec 30, 1991 · Abstract. A group contribution equation of state called PSRK (Predictive Soave-Redlich-Kwong) which is based on the Soave-Redlich-Kwong equation (Soave, 1972) has been developed. It uses the UNIFAC method to calculate the mixture parameter a and includes all already existing UNIFAC parameters. This concept makes use of recent …

Jan 1, 1987 · M.-J. Huron, G.-N. Dufour, J. Vidal. Vapor-liquid-equilibrium and critical-loci-curve calculations with the Soave equation for hydrocarbon systems with carbon dioxide and hydrogen sulfide. Fluid Phase Equilibria, 1 (1978), pp. 247-265. View PDF View article Google Scholar. Ikonomou and Donohue, 1986.Aug 27, 2014 · Read the signs and get a feel for what the Huron River meant to the late 19th and early to mid 20th century economy. It is an easy walk on a huge wide “sidewalk”to an observation point with a free viewer to take in the scenery. It’s accessible too. On a clear day one can see Cedar Point and the islands to the west and the Avon point to ...M.J. Huron, J. Vidal New mixing rules in simple equations of state for representing vapour–liquid equilibria of strongly non-ideal mixtures Fluid Phase Equilib , 3 ( 4 ) ( 1979 ) , pp. 255 - 271

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