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Application of the Perturbed-Chain SAFT Equation of State to Associating Systems
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26
References
2002
Year
EngineeringPerturbed-chain Saft EquationExperimental ThermodynamicsGeometric Singular Perturbation TheoryChemistryAssociating SystemsSimple LiquidSolution (Chemistry)StabilityThermodynamic ModellingPc−saft EquationMolecular ThermodynamicsSystems EngineeringAnalytical ChemistryThermodynamicsPerturbation MethodDiscrete Dynamical SystemPhysical ChemistryMixing RulesPerturbed-chain SaftSingularly Perturbed ProblemPhase EquilibriumChemical KineticsSystem Dynamic
PC‑SAFT is used to model associating substances, requiring five pure‑component parameters, two of which describe association. The study applies PC‑SAFT to pure associating components and to vapor‑liquid and liquid‑liquid equilibria of binary mixtures of associating substances. Parameters for 18 associating substances were obtained by correlating vapor‑pressure and liquid‑density data; for mixtures, a single dispersion interaction parameter (kij) suffices, with simple mixing rules for multiple associating compounds, enabling simultaneous prediction of vapor‑liquid and liquid‑liquid equilibria. Comparison with an earlier SAFT version shows that PC‑SAFT yields accurate predictions for pure substances.
The perturbed-chain SAFT (PC−SAFT) equation of state is applied to pure associating components as well as to vapor−liquid and liquid−liquid equilibria of binary mixtures of associating substances. For these substances, the PC−SAFT equation of state requires five pure-component parameters, two of which characterize the association. The pure-component parameters were identified for 18 associating substances by correlating vapor pressure and liquid density data. A comparison to an earlier version of SAFT confirms the good results for pure substances. When only one associating compound is present in a mixture, the PC−SAFT equation of state does not require mixing rules for the association term. Using one binary interaction parameter kij for the dispersion term only, the model was applied to azeotropic and nonazeotropic vapor−liquid equilibria at low and at high pressures, as well as to liquid−liquid equilibria. Simple mixing and combining rules were adopted for mixtures with more than one associating compound, introducing no additional binary interaction parameter. The simultaneous description of liquid−liquid and vapor−liquid equilibrium was also possible with a single kij parameter.
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