AIChE Journal · 1978 · 249 citations · 14 references
Natural SciencesChemical EngineeringPetroleum EngineeringPhysical ChemistryPolymer ChemistryThermodynamicsEquations Of StateFluid PropertiesMixture ThermodynamicsPhase DiagramsPhase EquilibriaThermodynamics Of Phase EquilibriaBinary MixturesGas MixturesMixture Equations Of StateNatural GasOil RefiningPolymer Solution ThermodynamicsRefiningThermodynamic Analysis
The perturbed‑hard‑chain theory synthesizes polymer solution theories of Flory and Prigogine with perturbed‑hard‑sphere theories of Alder, Barker, and Henderson. The study modifies Beret's perturbed‑hard‑chain theory for pure fluids to improve pure‑component predictions and extends it to multicomponent mixtures. The authors develop an equation of state applicable to simple and complex molecules, enabling calculation of gas and liquid phase properties, and extend the theory to mixtures using a one‑fluid model that does not assume random mixing. The theory has been applied to most fluids in natural‑gas and petroleum refining, yielding good agreement with experimental vapor pressures, liquid densities, enthalpies, and K factors, with parameters for 45 pure components and over 60 binary mixtures, and requiring no extra parameters for ternary or higher mixtures.
Abstract Perturbed‐hard‐chain theory for pure fluids, proposed previously by Beret, is modified slightly to yield better pure‐component results. More important, it is extended to multicomponent mixtures. The perturbed‐hard‐chain theory is a synthesis of the polymer solution theories of Flory and Prigogine and the perturbed‐hard‐sphere theories of Alder and Barker and Henderson. The resulting equation of state is applicable to simple as well as complex molecules (for example, heptane, naphthalene, polystyrene). It can be used to calculate both gas and liquid phase properties. Extension of perturbed‐hard‐chain theory to mixtures is based on a one‐fluid model without, however, making the usual assumption of random mixing. The perturbed‐hard‐chain theory has been applied to most fluids commonly encountered in natural‐gas and petroleum refining operations. The theory gives good agreement with experiment for pure‐component and fluid‐mixture properties including vapor pressures, liquid densities, enthalpies, and K factors. Molecular parameters have been obtained for forty‐five pure components and for more than sixty binary mixtures. Ternary and higher mixtures require no additional parameters.
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Statistical Mechanics of Fluid Mixtures
John G. Kirkwood · The Journal of Chemical Physics · 1935 · 3.5K citations
Natural Sciences, Chemistry, Physics +16