A sharp interface method for coupling multiphase flow, heat transfer and multicomponent mass transfer with interphase diffusion

Abstract Mixing of partially miscible fluids plays an important role in many physical and chemical processes. The modeling complexities lie in the tight coupling of the multiphase flow, heat transfer and multicomponent mass transfer, as well as diffusions across the phase interface. We present a sharp interface method for modeling such process. The non-ideal equation of state is used to compute the fluid properties such as density, fugacity and enthalpy, and to predict phase equilibrium composition. The phase interface location is tracked using the phase propagation velocity. A third-order one-sided finite difference scheme using a variable grid size according to the interface location is utilized to discretize the partial derivatives immediately next to the interface, while a second-order central scheme is used for the bulk of fluids. An optimization method, the Nelder–Mead method, is applied to search for (1) the phase compositions on both sides of the interface, and (2) the phase propagation velocity based on the coupling of the multicomponent phase equilibrium and the species' balance across the interface. The temperature at the interface is determined by the energy balance. Numerical results are used to demonstrate the convergence of our method and show its capability to simulate the mixing of multicomponent partially miscible fluids.

[1]  U. Deiters A modification of Newton-Raphson algorithm for phase equilibria calculations using numerical differentiation of the gibbs energy , 1985 .

[2]  Fred Landis,et al.  Numerical and Machine Solutions of Transient Heat-Conduction Problems Involving Melting or Freezing: Part I—Method of Analysis and Sample Solutions , 1959 .

[3]  Jean-Noël Jaubert,et al.  VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method , 2004 .

[4]  Dan Hancu,et al.  Green processing using ionic liquids and CO2 , 1999, Nature.

[5]  D. Klingenberg,et al.  Multicomponent diffusion—A brief review , 2013 .

[6]  A. Sunol,et al.  Multicomponent interphase diffusion of carbon dioxide¿methanol¿water under near-critical conditions , 2004 .

[7]  J. Prausnitz,et al.  Computer calculations for high-pressure vapor-liquid equilibria , 1968 .

[8]  L. Höglund,et al.  On the Numerical Treatment of Moving Boundary Problems , 1992 .

[9]  A. Ghoniem,et al.  Mixing of single-component hydrocarbon droplets and water at supercritical or near-critical conditions , 2012 .

[10]  R. Stryjek,et al.  PRSV: An improved peng—Robinson equation of state for pure compounds and mixtures , 1986 .

[11]  Hongqin Liu,et al.  New equations for tracer diffusion coefficients of solutes in supercritical and liquid solvents based on the Lennard-Jones fluid model , 1997 .

[12]  N. Berkowitz,et al.  Extraction of oil sand bitumens with supercritical water , 1990 .

[13]  J. Prausnitz Computer calculations for multicomponent vapor-liquid and liquid-liquid equilibria , 1980 .

[14]  A. Ghoniem,et al.  Simulation of supercritical water–hydrocarbon mixing in a cylindrical tee at intermediate Reynolds number: Formulation, numerical method and laminar mixing , 2014 .

[15]  G. Somorjai,et al.  High-performance hybrid oxide catalyst of manganese and cobalt for low-pressure methanol synthesis , 2015, Nature Communications.

[16]  Chao Yang,et al.  Numerical simulation of interphase mass transfer with the level set approach , 2005 .

[17]  P. Dyson,et al.  Direct synthesis of formic acid from carbon dioxide by hydrogenation in acidic media , 2014, Nature Communications.

[18]  M. J. Cocero,et al.  Mathematical modeling of the mass transfer from aqueous solutions in a supercritical fluid during particle formation , 2007 .

[19]  R. Privat,et al.  Predicting the Phase Equilibria, Critical Phenomena, and Mixing Enthalpies of Binary Aqueous Systems Containing Alkanes, Cycloalkanes, Aromatics, Alkenes, and Gases (N2, CO2, H2S, H2) with the PPR78 Equation of State , 2013 .

[20]  J. S. Rowlinson,et al.  Molecular Thermodynamics of Fluid-Phase Equilibria , 1969 .

[21]  Eberhard Bänsch,et al.  A subspace projection method for the implementation of interface conditions in a single-drop flow problem , 2013, J. Comput. Phys..

[22]  D. Peng,et al.  A New Two-Constant Equation of State , 1976 .

[23]  David Shan-Hill Wong,et al.  A theoretically correct mixing rule for cubic equations of state , 1992 .

[24]  K. E. Starling,et al.  Generalized multiparameter correlation for nonpolar and polar fluid transport properties , 1988 .

[25]  H. Inomata,et al.  Measurements of Water^|^ndash;Heavy Oil Phase Equilibrium for Supercritical Water Upgrading Process , 2014 .

[26]  A. Ghoniem,et al.  A Group Contribution Pseudocomponent Method for Phase Equilibrium Modeling of Mixtures of Petroleum Fluids and a Solvent , 2015 .

[27]  A. Ghoniem,et al.  Fractionation of multi-component hydrocarbon droplets in water at supercritical or near-critical conditions , 2012 .

[28]  Kyu Hwan Oh,et al.  Numerical Treatment of the Moving Interface in Diffusional Reactions , 1996 .

[29]  M. G. Kesler,et al.  Improve Prediction of Enthalpy of Fractions , 1976 .

[30]  F. Ng,et al.  Upgrading of asphalt with and without partial oxidation in supercritical water , 2003 .

[31]  Barbara L. Knutson,et al.  Supercritical fluids as solvents for chemical and materials processing , 1996, Nature.

[32]  A. Ghoniem,et al.  Impact of non-ideality on mixing of hydrocarbons and water at supercritical or near-critical conditions , 2015 .

[33]  Jean-Noël Jaubert,et al.  Extension of the PPR78 model (Predictive 1978, Peng-Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing naphtenic compounds , 2005 .

[34]  Byung-Ik Lee,et al.  A generalized thermodynamic correlation based on three‐parameter corresponding states , 1975 .

[35]  L. W. Holm CO2 Flooding: Its Time Has Come , 1982 .

[36]  Rajamani Krishna,et al.  THE MAXWELL-STEFAN FORMULATION OF IRREVERSIBLE THERMODYNAMICS FOR SIMULTANEOUS HEAT AND MASS TRANSFER , 1979 .