![]() Treats the attractive term parameter as a variable regressed by two straight State using a newly developed variable parameter ‘a’ approach (VPAA) which 3 p.Ī suitable Equation of State (EOS) was developedįor multi component, multi phase systems from the Peng-Robinson Equation of 1981 Schaum’s Outline Series New York: McGraw Hill 1981. Theory and problems of advanced calculus. Mathematical methods in chemical engineering. On the dangers of ‘tuning’ equation of state parameters. Perdersen KS, Thomassen P, Fredenslund A. A pa rameter-based approach for two-phase equilibrium prediction with cubic equations of state. Cubic equation of state and VLE calculations. ![]() A density correction for the Peng-Robinson equation of state. Deterioration in performance of mixing rules in phase behavior modeling of high density reservoir fluids. (1993) A comprehensive comparison of mixing rules for calculation of phase equilibria in complex systems. Stability limit determination for pure compounds. Phase equilibrium calculations: What is easy and what is difficult. Application of a reduction method to phase equilibria calculations. Application of the tangent plane criterion to saturation pressure and temperature computations. Fast and robust algorithm for compositional modeling: Part I – Stability analysis testing. Reservoir fluid phase behavior and volumetric prediction with equations of state. The isothermal flash problem Part I: Stability. Gibbs energy analysis of phase equilibrium. ![]() A modified equation of state for gas condensate systems. Three parameter modification of the Peng-Robinson equation of state to improve volumetric prediction. A new cubic equation of state for fluids and fluid mixtures. ![]() Introduction to Chemical Engineering Thermodynamics. PVT and phase behavior of petroleum reservoir fluids. ![]()
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