A sharp interface method for coupling multiphase flow, heat transfer and multicomponent mass transfer with interphase diffusion
暂无分享,去创建一个
[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 .