New initialization procedures from phase stability testing in three-phase flash calculations for CO2-hydrocarbon mixtures

Phase equilibrium calculations play an important role in a wide variety of applications in chemical and petroleum engineering. In this work, we focus on CO 2 -hydrocarbon mixtures, with applications ranging from enhanced oil recovery processes to CO 2 storage. In compositional reservoir simulation, both robustness and efficiency are of utmost importance. The conventional approach for multiphase equilibrium consists of a sequence of phase stability and flash calculations. At each level of the stepwise process, stability testing is performed starting from several initial guesses; therefore, reducing the number of stability calls and using judiciously the information from stability to initialize a phase split are key points in developing an efficient stability-flash algorithm. Two new initialization strategies for multiphase flash calculations are proposed. The first one (improved stepwise initialization) follows the conventional procedure, but uses additional initial guesses. In the second one (improved multiple initialization), a three-phase split is initiated if at least three minima of the tangent plane distance (TPD) function are detected by stability analysis of feed composition. Both proposed methods are using all information from phase stability testing at each stage. Unlike in previous formulations, compositions at all minima of the TPD function, including trivial and positive TPDs are used to generate initial equilibrium constants. Highly robust routines are used, based on successive substitution iterations (SSI) in early iteration stages, followed by Newton iterations with modified Cholesky factorization and line search, in both stability and flash calculations. The proposed methods are tested and compared with the conventional procedure for several benchmark mixtures from the literature, containing hydrocarbon components and CO 2 . Phase diagrams are constructed in the P - Z plane, focusing on the number of stationary points of the TPD functions found in each step of the multiphase stability-flash algorithm and on how they must be efficiently used in initialization. For all the test mixtures, in the proposed stability-flash strategy, the number of calls of the stability and flash routines and the number of iterations in flash calculations are significantly reduced as compared to previous approaches, recommending the new approach as a useful tool in compositional simulation.

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Publication Details

Journal
Fluid Phase Equilibria
Published
2025-12-13
DOI
https://doi.org/10.1016/j.fluid.2025.114653
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
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article

New initialization procedures from phase stability testing in three-phase flash calculations for CO2-hydrocarbon mixtures

Denis Voskov, Michiel Wapperom, Dan Vladimir Nichita, Juan Heringer et al.
Fluid Phase Equilibria
Phase Equilibria and Thermodynamics
article

New initialization procedures from phase stability testing in three-phase flash calculations for CO2-hydrocarbon mixtures

Denis Voskov, Michiel Wapperom, Dan Vladimir Nichita, Juan Heringer, Catinca Secuianu
article en

Abstract

Phase equilibrium calculations play an important role in a wide variety of applications in chemical and petroleum engineering. In this work, we focus on CO 2 -hydrocarbon mixtures, with applications ranging from enhanced oil recovery processes to CO 2 storage. In compositional reservoir simulation, both robustness and efficiency are of utmost importance. The conventional approach for multiphase equilibrium consists of a sequence of phase stability and flash calculations. At each level of the stepwise process, stability testing is performed starting from several initial guesses; therefore, reducing the number of stability calls and using judiciously the information from stability to initialize a phase split are key points in developing an efficient stability-flash algorithm. Two new initialization strategies for multiphase flash calculations are proposed. The first one (improved stepwise initialization) follows the conventional procedure, but uses additional initial guesses. In the second one (improved multiple initialization), a three-phase split is initiated if at least three minima of the tangent plane distance (TPD) function are detected by stability analysis of feed composition. Both proposed methods are using all information from phase stability testing at each stage. Unlike in previous formulations, compositions at all minima of the TPD function, including trivial and positive TPDs are used to generate initial equilibrium constants. Highly robust routines are used, based on successive substitution iterations (SSI) in early iteration stages, followed by Newton iterations with modified Cholesky factorization and line search, in both stability and flash calculations. The proposed methods are tested and compared with the conventional procedure for several benchmark mixtures from the literature, containing hydrocarbon components and CO 2 . Phase diagrams are constructed in the P - Z plane, focusing on the number of stationary points of the TPD functions found in each step of the multiphase stability-flash algorithm and on how they must be efficiently used in initialization. For all the test mixtures, in the proposed stability-flash strategy, the number of calls of the stability and flash routines and the number of iterations in flash calculations are significantly reduced as compared to previous approaches, recommending the new approach as a useful tool in compositional simulation.

Fluid Phase EquilibriaVol. 604
Centre National de la Recherche Scientifique (FR), Université de Pau et des Pays de l'Adour (FR), Universitatea Națională de Știință și Tehnologie Politehnica București (RO), Stanford University (US), Delft University of Technology (NL)
Openalex Percentile: Top 61%
Phase Equilibria and Thermodynamics
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