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[1] K.D.L. James P. Kohn, Solubility of Hydrocarbons in Cryogenic Lng and Ngl Mixtures, (1976). [2] J.P. Kohn, K.D. Luks, Solubility of Hydrocarbons in Cryogenic in Lng and Ngl Mixtures, (1976). [3] J.P. Kohn, K.D. Luks, Solubility of Heavier Hydrocarbons in Liquid Methane, (1978). [4] J.P. Kohn, K.D. Luks, Solubility of Hydrocarbons in Cryogenic in Lng and Ngl Mixtures, (1978). [5] J.P. Kohn, K.D. Luks, P.H. Liu, D.L. Tiffin, Three-Phase Solid-Liquid-Vapor Equilibria of the Binary Hydrocarbon Systems Methane-N-Octane and Methane-Cyclohexane, Journal of Chemical and Engineering Data, Vol. 22 (1977) 419-421. [6] K.D. Luks, J.P. Kohn, P.H. Liu, A.A. Kulkarni, Solubility of Hydrocarbons in Cryogenic Ngl and Lng, Hydrocarbon Processing 54 (1975) 181-184. [7] K.L. Bjaanes, Literature Review and Evaluation of the Umr-Pru Eos for Predicting Solid Formation in Low Temperature Natural Gas Processing, (2013). [8] D.L. Tiffin, K.D. Luks, J.P. Kohn, Solubility Enhancement of Solid Hydrocarbons in Liquid Methane Due to the Presence of Ethane, Advances in Cryogenic Engineering. vol. 23 (1978) 538-543 [9] V. Louli, C. Boukouvalas, E. Voutsas, K. Magoulas, D. Tassios, Application of the Umr-Pru Model to Multicomponent Systems: Prediction of the Phase Behavior of Synthetic Natural Gas and Oil Systems, Fluid Phase Equilibria 261 (2007) 351-358. [10] S.V.G. Jie Yu, Jame Yao, Guang Lee, Prediction of Heavy Hydrocarbon Solubility on Lng, (2015). [11] S.T. Lin, S.I. Sandler, A Priori Phase Equilibrium Prediction from a Segment Contribution Solvation Model (Vol 41, Pg 903, 2004), Industrial & Engineering Chemistry Research 43 (2004) 1322-1322. [12] M.T. Lee, S.T. Lin, Prediction of Mixture Vapor-Liquid Equilibrium from the Combined Use of Peng-Robinson Equation of State and Cosmo-Sac Activity Coefficient Model through the Wong-Sandler Mixing Rule, Fluid Phase Equilibria 254 (2007) 28-34. [13] D. Peng, D.B. Robinson, A New Two-Constant Equation of State, Industrial & Engineering Chemistry Fundamentals 15 (1976) 59-64. [14] D.S.H. Wong, S.I. Sandler, A Theoretically Correct Mixing Rule for Cubic Equations of State, Aiche Journal 38 (1992) 671-680. [15] C.M. Hsieh, S.T. Lin, First-Principles Predictions of Vapor-Liquid Equilibria for Pure and Mixture Fluids from the Combined Use of Cubic Equations of State and Solvation Calculations, Industrial & Engineering Chemistry Research 48 (2009) 3197-3205. [16] R. Stryjek, J.H. Vera, Prsv - an Improved Peng-Robinson Equation of State for Pure Compounds and Mixtures, Canadian Journal of Chemical Engineering 64 (1986) 323-333. [17] M.L. Michelsen, A Modified Huron-Vidal Mixing Rule for Cubic Equations of State, Fluid Phase Equilibria 60 (1990) 213-219. [18] C.M. Hsieh, S.T. Lin, First-Principles Prediction of Vapor-Liquid-Liquid Equilibrium from the Pr Plus Cosmosac Equation of State, Industrial & Engineering Chemistry Research 50 (2011) 1496-1503. [19] J.C. de Hemptinne, Benzene Crystallization Risks in the Liquefin Liquefied Natural Gas Process, Process Safety Progress 24 (2005) 203-212. [20] H. Fatoorehchi, H. Abolghasemi, R. Rach, A New Parametric Algorithm for Isothermal Flash Calculations by the Adomian Decomposition of Michaelis-Menten Type Nonlinearities, Fluid Phase Equilibria 395 (2015) 44-50. [21] J.S. Duan, Recurrence Triangle for Adomian Polynomials, Applied Mathematics and Computation 216 (2010) 1235-1241. [22] G. Soave, Application of Equations of State and the Theory of Group Solutions to Phase-Equilibrium Prediction, Fluid Phase Equilibria 87 (1993) 23-35. [23] F. Kurata, Solubility of Heavier Hydrocarbons in Liquid Methane, (1975). [24] G.P. Kuebler, C. McKinley, Solubility of Solid Benzene, Toluene, N-Hexane, and N-Heptane in Liquid Methane, Advances in Cryogenic Engineering. vol. 19 (1995) 320-326. [25] G. Soave, Equilibrium Constants from a Modified Redlich-Kwong Equation of State, Chemical Engineering Science 27 (1972) 1197-&. [26] K.D. Luks, J.D. Hottovy, J.P. Kohn, Three-Phase Solid-Liquid-Vapor Equilibriums in the Binary Hydrocarbon Systems Methane-N-Hexane and Methane-Benzene, Journal of Chemical & Engineering Data, vol. 26 (1981) 402-403. [27] J. Shim, J.P. Kohn, Multiphase and Volumetric Equilibria of Methane-N-Hexane Binary System at Temperatures between -110° and 150° C, Journal of Chemical & Engineering Data, vol. 7 (1962) 3-8.
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