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Partial miscibility behavior of the methane + ethane + n-docosane and the methane + ethane + n-tetradecylbenzene ternary mixtures

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    Partial miscibility behavior of the methane + ethane + n-docosane and the methane + ethane + n-tetradecylbenzene ternary mixtures
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    Cite this: J. Chem. Eng. Data 1989, 34, 1, 92–99
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    https://doi.org/10.1021/je00055a027
    Published January 1, 1989
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    This article is cited by 33 publications.

    1. Michel Milhet, Jérôme Pauly, João A.P. Coutinho and Jean-Luc Daridon. Solid−Liquid Equilibria under High Pressure of Nine Pure n-Alkylbenzenes. Journal of Chemical & Engineering Data 2008, 53 (1) , 233-237. https://doi.org/10.1021/je700529y
    2. Lydia E. Gutiérrez M. and, Kraemer D. Luks. Three-Phase Liquid−Liquid−Vapor Equilibria of the Binary Mixture Carbon Dioxide + 1-Methylnaphthalene. Journal of Chemical & Engineering Data 2001, 46 (3) , 679-682. https://doi.org/10.1021/je000322i
    3. Christopher M. Foreman and, Kraemer D. Luks. Partial Miscibility Behavior of the Ternary Mixture Carbon Dioxide + n-Tetradecane + Methanol. Journal of Chemical & Engineering Data 2000, 45 (2) , 334-337. https://doi.org/10.1021/je990209w
    4. Gaurav Kundu, Ashutosh Kumar. Optimized critical parameters for n-alkanes up to C100 for reliable multiphase behavior of hydrocarbon mixture using SRK EOS. Fluid Phase Equilibria 2021, 541 , 113037. https://doi.org/10.1016/j.fluid.2021.113037
    5. Ashutosh Kumar, Ryosuke Okuno. A New Algorithm for Multiphase Fluid Characterization for Solvent Injection. 2015https://doi.org/10.2118/175123-MS
    6. María José Tardón, José Matías Garrido, Héctor Quinteros-Lama, Andrés Mejía, Hugo Segura. Molar isopycnicity in heterogeneous binary mixtures. Fluid Phase Equilibria 2012, 336 , 84-97. https://doi.org/10.1016/j.fluid.2012.07.034
    7. . References. 2012, 265-307. https://doi.org/10.1002/9781118243350.refs
    8. Nadezhda A. Slavinskaya, Anton Zizin, Manfred Aigner. On Model Design of a Surrogate Fuel Formulation. Journal of Engineering for Gas Turbines and Power 2010, 132 (11) https://doi.org/10.1115/1.4000593
    9. A. Naderifar, B. Khodakarami, I. Zanganeh. New approach for the prediction of vapor–liquid equilibria in asymmetric systems using GE–EOS mixing rules. Fluid Phase Equilibria 2008, 271 (1-2) , 38-42. https://doi.org/10.1016/j.fluid.2008.07.002
    10. Laura Gil, Santos F. Otín, Jose Muñoz Embid, M. Asunción Gallardo, Sofía Blanco, Manuela Artal, Inmaculada Velasco. Experimental setup to measure critical properties of pure and binary mixtures and their densities at different pressures and temperatures. The Journal of Supercritical Fluids 2008, 44 (2) , 123-138. https://doi.org/10.1016/j.supflu.2007.11.003
    11. Jun Gao, Liu-Ding Li, Zhao-You Zhu, Shao-Gang Ru. Vapor–liquid equilibria calculation for asymmetric systems using Patel–Teja equation of state with a new mixing rule. Fluid Phase Equilibria 2004, 224 (2) , 213-219. https://doi.org/10.1016/j.fluid.2004.05.007
    12. J.M. Shaw, E. Béhar. SLLV phase behavior and phase diagram transitions in asymmetric hydrocarbon fluids. Fluid Phase Equilibria 2003, 209 (2) , 185-206. https://doi.org/10.1016/S0378-3812(03)00082-7
    13. L.E Gutiérrez, K.D Luks. Effect of cosolvents on solute separability between liquid phases in liquid–liquid–vapor ternary mixtures. Fluid Phase Equilibria 2003, 205 (1) , 89-102. https://doi.org/10.1016/S0378-3812(02)00273-X
    14. Lydia E Gutiérrez M, K.D Luks. Partial miscibility behavior of the ternary mixture carbon dioxide + 1-methylnaphthalene + acetone. Fluid Phase Equilibria 2002, 198 (1) , 29-36. https://doi.org/10.1016/S0378-3812(01)00735-X
    15. Qingyuan Yang, Chongli Zhong. A modified PSRK model for the prediction of the vapor–liquid equilibria of asymmetric systems. Fluid Phase Equilibria 2001, 192 (1-2) , 103-120. https://doi.org/10.1016/S0378-3812(01)00629-X
    16. C.M Foreman, K.D Luks. Partial miscibility behavior of the ternary mixture carbon dioxide+n-tetradecane+acetone. Fluid Phase Equilibria 2000, 169 (1) , 65-73. https://doi.org/10.1016/S0378-3812(99)00344-1
    17. Chongli Zhong, Hirokatsu Masuoka. Mixing rules for accurate prediction of vapor-liquid equilibria of gas/large alkane systems using SRK equation of state combined with unifac.. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 1996, 29 (2) , 315-322. https://doi.org/10.1252/jcej.29.315
    18. Tiffany A. Gricus, Kraemer D. Luks, Christi L. Patton. Liquid-liquid-vapor phase equilibrium behavior of binary xenon + 1-alkanol mixtures. Fluid Phase Equilibria 1995, 108 (1-2) , 219-229. https://doi.org/10.1016/0378-3812(95)02689-C
    19. Ralf Dohrn, Gerd Brunner. High-pressure fluid-phase equilibria: Experimental methods and systems investigated (1988–1993). Fluid Phase Equilibria 1995, 106 (1-2) , 213-282. https://doi.org/10.1016/0378-3812(95)02703-H
    20. Christi L. Patton, Kraemer D. Luks. Multiphase equilibria of the binary mixture xenon + 1-decanol. Fluid Phase Equilibria 1994, 98 , 201-211. https://doi.org/10.1016/0378-3812(94)80119-3
    21. Seung-Pyo Hong, Kimberly A. Green, Kraemer D. Luks. Solubility and volumetric behavior of methane and carbon dioxide plus C7+ pseudocomponents of an oil. Fluid Phase Equilibria 1994, 95 , 267-280. https://doi.org/10.1016/0378-3812(94)80073-1
    22. Seung-Pyo Hong, Kimberly A. Green, Kraemer D. Luks. Phase equilibria of the mixtures methane + n-hexane + n-hexatriacontane, methane + toluene + naphthalene, and methane + n-hexane + naphthalene. Fluid Phase Equilibria 1993, 87 (2) , 255-272. https://doi.org/10.1016/0378-3812(93)85030-P
    23. Christi L. Patton, K.D. Luks. Multiphase equilibrium behavior of the mixture ethane + 1-decanol + n-docosane. Fluid Phase Equilibria 1993, 85 , 181-190. https://doi.org/10.1016/0378-3812(93)80013-D
    24. Seung-Pyo Hong, Kraemer D. Luks. Multiphase equilibria of the mixture carbon dioxide + toluene + naphthalene. Fluid Phase Equilibria 1992, 74 , 133-144. https://doi.org/10.1016/0378-3812(92)85058-G
    25. Xue Fangyue, Th.W. De Loos, J.De Swaan Arons. The influence of nitrogen on fluid phase equilibria in the system ethane + n-decylbenzene up to 100 MPa. Fluid Phase Equilibria 1992, 71 (3) , 273-285. https://doi.org/10.1016/0378-3812(92)80003-R
    26. Seung-Pyo Hong, Kraemer D. Luks. Solid-Liquid-vapor phase equilibria of the mixture carbon dioxide + n-hexane + n-hexatrlacontanet. The Journal of Supercritical Fluids 1991, 4 (4) , 227-232. https://doi.org/10.1016/0896-8446(91)90015-X
    27. Daniel H. Lam, Adisak Jangkamolkulchai, Kraemer D. Luks. Liquid—liquid—vapor phase equilibrium behavior of certain binary nitrous oxide + n-alkanol mixtures. Fluid Phase Equilibria 1990, 60 (1-2) , 119-130. https://doi.org/10.1016/0378-3812(90)85046-D
    28. Daniel H. Lam, Adisak Jangkamolkulchai, Kraemer D. Luks. Liquid—liquid—vapor phase equilibrium behavior of certain binary carbon dioxide + n-alkanol mixtures. Fluid Phase Equilibria 1990, 60 (1-2) , 131-141. https://doi.org/10.1016/0378-3812(90)85047-E
    29. Daniel H. Lam, Adisak Jangkamolkulchai, Kraemer D. Luks. Liquid-liquid-vapor phase equilibrium behavior of certain binary ethane + n-alkanol mixtures. Fluid Phase Equilibria 1990, 59 (3) , 263-277. https://doi.org/10.1016/0378-3812(90)80003-T
    30. Zdenka Novosad. EOR by rich gas injection - the role of multiple liquid phases in crude oil-solvent miscibility development. Fluid Phase Equilibria 1989, 52 , 263-274. https://doi.org/10.1016/0378-3812(89)80332-2
    31. Melanie M. Miller, Kraemer D. Luks. Species separability in ternary multiphase systems. Fluid Phase Equilibria 1989, 52 , 275-282. https://doi.org/10.1016/0378-3812(89)80333-4
    32. Daniel H. Lam, Adisak Jangkamolkulchai, Kraemer D. Luks. Liquid—liquid—vapor phase equilibria behavior of certain binary nitrous oxide + n-alkylbenzene mixtures. Fluid Phase Equilibria 1989, 50 (1-2) , 165-174. https://doi.org/10.1016/0378-3812(89)80287-0
    33. Adisak Jangkamolkulchai, Daniel H. Lam, Kraemer D. Luks. Multiphase equilibria behavior of nitrous oxide +n-paraffin mixtures. Fluid Phase Equilibria 1989, 50 (1-2) , 175-187. https://doi.org/10.1016/0378-3812(89)80288-2
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    Cite this: J. Chem. Eng. Data 1989, 34, 1, 92–99
    Click to copy citationCitation copied!
    https://doi.org/10.1021/je00055a027
    Published January 1, 1989
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