2012
DOI: 10.5541/ijot.380
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Computation of liquid-vapor critical points for multi-component mixtures

Abstract: Liquid-vapor critical point for a thermodynamic mixture is an important parameter for the design of mixture transportation and processing. The classical critical points model for the multicomponent mixture is based on the tangent plane distance in terms of the Helmholtz energy. In this work, we have applied the damped Newton-Raphson scheme to solve the model using the critical temperature, critical specific volume and change in mole fraction of each component as independent variables. According to numerical ex… Show more

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Cited by 2 publications
(2 citation statements)
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“…More recently, Henderson et al (2010) have tested four different versions of the differential evolution algorithm, including a variant for calculating more than one critical point. Bonilla-Petriciolet (2006), and Jia et al (2012), also attacked the problem of the calculation of critical points using the Helmholtz free energy, but from the formulation proposed by Heidemann and Khalil (1980). Sánches-Mares and BonillaPetriciolet (2006) used the SA algorithm, and Jia et al (2012) employed a damped 4 Newton method.…”
Section: Introductionmentioning
confidence: 98%
“…More recently, Henderson et al (2010) have tested four different versions of the differential evolution algorithm, including a variant for calculating more than one critical point. Bonilla-Petriciolet (2006), and Jia et al (2012), also attacked the problem of the calculation of critical points using the Helmholtz free energy, but from the formulation proposed by Heidemann and Khalil (1980). Sánches-Mares and BonillaPetriciolet (2006) used the SA algorithm, and Jia et al (2012) employed a damped 4 Newton method.…”
Section: Introductionmentioning
confidence: 98%
“…Such limitations are true of all nonlinear solvers that are local in nature. Nevertheless, a significant amount of effort has been dedicated toward improving the convergence properties and overall efficiency of local solver implementations. These techniques are typically well suited for large‐scale reservoir and multiphase flow simulations where critical point calculations may be performed O(106) or more times each time‐step.…”
Section: Introductionmentioning
confidence: 99%