A five-parameter cubic equation of state for pure fluids and mixtures
Tài liệu tham khảo
Forero, 2016, A generalized cubic equation of state for non-polar and polar substances, Fluid Phase Equilib., 418, 74, 10.1016/j.fluid.2015.09.045
Kontogeorgis, 2010
Valderrama, 2010, The legacy of Johannes Diderik van der Waals, a hundred years after his nobel prize for physics, J. Supercrit. Fluids, 55, 415, 10.1016/j.supflu.2010.10.026
Valderrama, 2003, The state of the cubic equations of state, Ind. Eng. Chem. Res., 42, 1603, 10.1021/ie020447b
Lopez-Echeverry, 2017, Peng-Robinson equation of state: 40 years through cubics, Fluid Phase Equilib., 447, 39, 10.1016/j.fluid.2017.05.007
Soave, 1972, Equilibrium constants from a modified Redlich-Kwong equation of state, Chem. Eng. Sci., 27, 1197, 10.1016/0009-2509(72)80096-4
Peng, 1976, A new two-constant equation of state, Ind. Eng. Chem. Fundam., 15, 59, 10.1021/i160057a011
Patel, 1982, A new cubic equation of state for fluids and fluid mixtures, Chem. Eng. Sci., 37, 463, 10.1016/0009-2509(82)80099-7
Frey, 2013, Density-and-temperature-dependent volume translation for the SRK EOS: 2. Mixtures, Fluid Phase Equilib., 343, 13, 10.1016/j.fluid.2013.01.006
Abudour, 2012, Volume-translated Peng-Robinson equation of state for saturated and single-phase liquid densities, Fluid Phase Equilib., 335, 74, 10.1016/j.fluid.2012.08.013
Kumar, 2012, Critical parameters optimized for accurate phase behavior modeling for heavy n-alkanes up to C100 using the Peng-Robinson equation of state, Fluid Phase Equilib., 335, 46, 10.1016/j.fluid.2012.07.029
Li, 2011, Modified α function for the Peng-Robinson equation of state to improve the vapor pressure prediction of non-hydrocarbon and hydrocarbon compounds, Energy Fuels, 25, 215, 10.1021/ef100927z
Esmaeilzadeh, 2006, A new cubic equation of state for reservoir fluids, Fluid Phase Equilib., 239, 83, 10.1016/j.fluid.2005.10.013
Haghtalab, 2010, A new three-parameter cubic equation of state for calculation physical properties and vapor–liquid equilibria, Fluid Phase Equilib., 293, 209, 10.1016/j.fluid.2010.03.029
Kumar, 2011, Three parameter cubic equation of state for pure components of heavy oils, Can. J. Chem. Eng., 89, 869, 10.1002/cjce.20439
Kumar, 2013, A unique approach to predict accurate heavy oil density with new three parameter cubic equation of state, Can. J. Chem. Eng., 91, 391, 10.1002/cjce.21660
Martin, 1979, Cubic equations of state-which?, Ind. Eng. Chem. Fundam., 18, 81, 10.1021/i160070a001
Peneloux, 1982, A consistent correction for Redlich-Kwong-Soave volumes, Fluid Phase Equilib., 8, 7, 10.1016/0378-3812(82)80002-2
Jaubert, 2016, Note on the properties altered by application of a Peneloux-type volume translation to an equation of state, Fluid Phase Equilib., 419, 88, 10.1016/j.fluid.2016.03.012
Proust, 1993, Calculation of pure compound saturated enthalpies and saturated volumes with the PRSV equation of state. Revised κ1 parameters for alkanes, Can. J. Chem. Eng., 71, 292, 10.1002/cjce.5450710216
de SantAna, 1999, Evaluation of an improved volume translation for the prediction of hydrocarbon volumetric properties, Fluid Phase Equilib., 154, 193, 10.1016/S0378-3812(98)00441-5
Watson, 1986, Prediction of vapor pressures and saturated molar volumes with a simple cubic equation of state: part II: The van der waals – 711 EOS, Fluid Phase Equilib., 27, 35, 10.1016/0378-3812(86)87039-X
Tsai, 1998, Application of a volume-translated Peng-Robinson equation of state on vapor-liquid equilibrium calculations, Fluid Phase Equilib., 145, 193, 10.1016/S0378-3812(97)00342-7
Shi, 2018, An improved volume translation strategy for PR EOS without crossover issue, Fluid Phase Equilib., 10.1016/j.fluid.2018.01.034
Abbot, 1973, Cubic equations of state, AIChE J., 19, 596, 10.1002/aic.690190327
Jan, 1991, A new four-parameter cubic equation of state for fluids, Can. J. Chem. Eng., 69, 992, 10.1002/cjce.5450690423
Trebble, 1987, Development of a new four parameter cubic equation of state, Fluid Phase Equilib., 35, 1, 10.1016/0378-3812(87)80001-8
Adachi, 1983, A new four parameter equation of state, Fluid Phase Equilib., 11, 29, 10.1016/0378-3812(83)85004-3
Ghoderao, 2018, A four-parameter cubic equation of state for pure compounds and mixtures, Chem. Eng. Sci., 190, 173, 10.1016/j.ces.2018.06.010
Ghoderao, 2018, A four parameter cubic equation of state with temperature dependent covolume parameter, Chin. J. Chem. Eng.
Kumar, 1982, The most general density-cubic equation of state: application to pure nonpolar fluids, Ind. Eng. Chem. Fundam., 21, 255, 10.1021/i100007a011
Adachi, 1986, Development of a five-parameter cubic equation of state, Fluid Phase Equilib., 28, 119, 10.1016/0378-3812(86)85073-7
Anderko, 2000, Cubic and generalized van der Waals equations
Benedict, 1940, An empirical equation for thermodynamic properties of light hydrocarbons and their mixtures I. methane, ethane, propane and n-butane, J. Chem. Phys., 8, 334, 10.1063/1.1750658
Duan, 2004, A new cubic equation of state and its applications to the modeling of vapor-liquid equilibria and volumetric properties of natural fluids, Geochim. Cosmochim. Acta, 68, 2997, 10.1016/j.gca.2003.11.034
Deiters, 2002, Calculation of densities from cubic equations of state, AIChE J., 48, 882, 10.1002/aic.690480421
Redlich, 1949, On the thermodynamics of solutions. V. An equation of state. Fugacities of gaseous solutions, Chem. Rev., 44, 233, 10.1021/cr60137a013
Carnahan, 1969, Equation of state for nonattracting rigid spheres, J. Chem. Phys., 51, 635, 10.1063/1.1672048
Carnahan, 1972, Intermolecular repulsions and the equation of state for fluids, AIChE J., 18, 1184, 10.1002/aic.690180615
Yelash, 1999, Closed-loop critical curves in simple hard-sphere van der Waals-fluid models consistent with the packing fraction limit, J. Chem. Phys., 110, 3079, 10.1063/1.477904
Geana, 2000, Thermodynamic properties of pure fluids using the GEOS3C equation of state, Fluid Phase Equilib., 174, 51, 10.1016/S0378-3812(00)00417-9
Nasrifar, 2001, A new cubic equation of state for simple fluids: pure and mixture, Fluid Phase Equilib., 190, 73, 10.1016/S0378-3812(01)00592-1
Eu, 2003, Thermodynamically consistent equation of state of hard sphere fluids, J. Chem. Phys., 118, 2264, 10.1063/1.1533786
Joshipura, 2010, Modeling vapour pressure using compound specific cohesion factor relationship, J. Taiwan Inst. Chem. Eng., 41, 570, 10.1016/j.jtice.2010.01.006
Le, 2014, On the imperative need to use a consistent α-function for the prediction of pure-compound supercritical properties with a cubic equation of state, Fluid Phase Equilib., 445, 45
Le Guennec, 2016, A consistency test for α-functions of cubic equations of state, Fluid Phase Equilib., 427, 513, 10.1016/j.fluid.2016.07.026
Forero, 2015, A modified Patel-Teja cubic equation of state. Part II: Parameters for polar substances and its mixtures, Fluid Phase Equilib., 364, 75, 10.1016/j.fluid.2013.12.009
Green, 2007
Linstrom, P.J. 2005. National institute of standard and technology. Standard reference Database Number 69. <http://webbook.nist.gov/chemistry/fluid/> (accessed August 3, 2017).
Shemilt, 1959, Thermodynamic properties of some organic compounds. I. PVT relationships and calculated thermodynamic properties for normal butanol, Can. J. Chem. Eng., 37, 142, 10.1002/cjce.5450370402
Kwak, 1986, Waals mixing rules for cubic equations of state. Applications for supercritical fluid extraction modelling, Chem. Eng. Sci., 41, 1303, 10.1016/0009-2509(86)87103-2
Kalra, 1977, The equilibrium phase properties of the ethane-hydrogen sulfide system at subambient temperatures, J. Chem. Eng. Data., 22, 85, 10.1021/je60072a005
Wichterle, 1972, Vapor-liquid equilibrium of methane-propane system at low temperatures and high pressures, J. Chem. Eng. Data, 17, 4, 10.1021/je60052a019
Wichterle, 1972, Vapor-liquid equilibrium of methane-ethane system at low temperatures and high pressures, J. Chem. Eng. Data, 17, 9, 10.1021/je60052a022
Kahre, 1974, Low-temperature K data for methane-n-butane, J. Chem. Eng. Data, 19, 67, 10.1021/je60060a014
Blanc, 1988, Vapor-liquid equilibria for the ethane-propane system at low temperature, J. Chem. Eng. Data, 33, 111, 10.1021/je00052a015
Lhotak, 1981, Vapor-liquid equillibria in the ethane-n butane system at high pressures, Fluid Phase Equilib., 6, 229, 10.1016/0378-3812(81)85006-6
Zais, 1970, Vapor-liquid equilibria in the ethane-n-hexane system, J. Chem. Eng. Data, 15, 253, 10.1021/je60045a024
Kayukawa, 2005, Vapor-liquid equilibrium (VLE) properties for the binary systems propane (1) + n-butane (2) and propane (1) + isobutane (3), J. Chem. Eng. Data, 50, 579, 10.1021/je0496701
Lee, 2009, Isothermal vapor–liquid equilibria for binary mixtures of hexane, heptane, octane, nonane and cyclohexane at 333.15 K, 343.15 K and 353.15 K, J. Taiwan Inst. Chem. Eng., 40, 573, 10.1016/j.jtice.2009.03.002
Dejoz, 1996, Isobaric vapor−liquid equilibria for binary systems composed of octane, decane, and dodecane at 20 kPa, J. Chem. Eng. Data, 41, 93, 10.1021/je950177m
Ho, 2006, Measurement of vapor–liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290), Fluid Phase Equilib., 245, 63, 10.1016/j.fluid.2006.03.009
Laugier, 1996, High-pressure vapor-liquid equilibria for ethylene + 4-methyl-1-pentene and 1-butene + 1-hexene, J. Chem. Eng. Data, 41, 282, 10.1021/je9502509
Webster, 2001, Vapor-liquid equilibria for the methane-propane-carbon dioxide systems at 230 K and 270 K, J. Chem. Eng. Data, 46, 759, 10.1021/je000307d
Gupta, 2012, Isobaric vapor–liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa, Fluid Phase Equilib., 313, 190, 10.1016/j.fluid.2011.10.009
Diaz, 2002, Phase equilibria behaviour of n-heptane with o-xylene, m-xylene, p-xylene and ethylbenzene at 101.3 kPa, J. Chem. Thermodyn., 34, 1975, 10.1016/S0021-9614(02)00227-6
Somait, 1978, Liquid-vapor equilibria at 270.00 K for systems containing nitrogen, methane, and carbon dioxide, J. Chem. Eng. Data, 23, 301, 10.1021/je60079a019
Malewskl, 1989, High-pressure vapor-liquid equilibria of the binary mixtures nitrogen 4- n-butane and argon + n-butane, J. Chem. Eng. Data, 34, 424, 10.1021/je00058a015
Gupta, 1980, Liquid-vapor equilibria for the N2 + CH4 + C, H, system from 260 to 280 K, J. Chem. Eng. Data, 25, 313, 10.1021/je60087a016
Day, 1999, Phase equilibrium of ethanol + CO2 and acetone + CO2 at elevated pressures, J. Chem. Eng. Data, 44, 365, 10.1021/je9804890
Goral, 2004, Recommended vapor–liquid equilibrium data. Part 3. Binary alkanol–aromatic hydrocarbon, J. Phys. Chem. Ref. Data, 33, 959, 10.1063/1.1760761
Smolen, 1991, Vapor-Liquid equilibrium data for the NH3-H2O system and its description with a modified cubic equation of state, J. Chem. Eng. Data, 36, 202, 10.1021/je00002a017
