High pressure phase behavior modeling of asymmetric alkane plus alkane binary systems with the RKPR EOS

被引:19
作者
Cismondi Duarte, M. [1 ,2 ]
Galdo, M. V. [2 ]
Gomez, M. J. [2 ]
Tassin, N. G. [2 ]
Yanes, M. [2 ]
机构
[1] Univ Nacl Cordoba, CONICET, IDTQ PLAPIQUI, RA-5000 Cordoba, Argentina
[2] Incubadora Empresas UNC, Phasety, Cordoba, Argentina
关键词
Methane; Ethane; Hydrocarbons; High pressure phase behavior; RKPR; EQUATION-OF-STATE; VAPOR-LIQUID-EQUILIBRIA; HEAVY NORMAL-PARAFFINS; NATURAL-GAS; CONDENSATION BEHAVIOR; SOLID-FLUID; MIXTURES; METHANE; ETHANE; TEMPERATURES;
D O I
10.1016/j.fluid.2013.09.039
中图分类号
O414.1 [热力学];
学科分类号
摘要
Very asymmetric hydrocarbon mixtures present an interesting academic challenge for their modeling. In addition, they are becoming more important technologically, since the world oil reserves are becoming heavier in average. The RKPR EOS was developed in recent years in order to consider asymmetric systems and allow for a good representation of densities for different types of compounds while maintaining the relative simplicity of cubic equations of state. In this work the RKPR EOS is applied for the first time for the correlation of phase behavior in the series of binary systems methane + n-alkane and ethane + n-alkane. In addition to the use of attractive and repulsive interaction parameters with quadratic mixing rules, the role of the extra degree of freedom that the RKPR model offers for setting the pure compound parameters was also examined. A new table of RKPR pure compound parameters was defined for n-alkanes. A comparative study was made with the Peng-Robinson EOS, based on following the same optimization procedure for interaction parameters. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:125 / 135
页数:11
相关论文
共 34 条
[1]   Thermodynamic properties of light synthetic natural gas mixtures using the RK-PR cubic equation of state [J].
Aparicio Martinez, Santiago ;
Hall, Kenneth R. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (10) :3684-3692
[2]   Dynamic Thermodynamics with Internal Energy, Volume, and Amount of Moles as States: Application to Liquefied Gas Tank [J].
Arendsen, A. R. J. ;
Versteeg, G. F. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (06) :3167-3176
[3]   Apparatus for phase equilibrium measurements at high temperatures and pressures [J].
Chylinski, K ;
Cebola, MJ ;
Meredith, A ;
Saville, G ;
Wakeham, WA .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2002, 34 (10) :1703-1728
[4]   Development and application of a three-parameter RK-PR equation of state [J].
Cismondi, M ;
Mollerup, J .
FLUID PHASE EQUILIBRIA, 2005, 232 (1-2) :74-89
[5]   Phase Equilibria of CO2+n-Alkane Binary Systems in Wide Ranges of Conditions: Development of Predictive Correlations Based on Cubic Mixing Rules [J].
Cismondi, Martin ;
Rodriguez-Reartes, Sabrina B. ;
Milanesio, Juan M. ;
Zabaloy, Marcelo S. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (17) :6232-6250
[6]   Equation of state modeling of the phase equilibria of asymmetric CO2 + n-alkane binary systems using mixing rules cubic with respect to mole fraction [J].
Cismondi, Martin ;
Mollerup, Jorgen M. ;
Zabaloy, Marcelo S. .
JOURNAL OF SUPERCRITICAL FLUIDS, 2010, 55 (02) :671-681
[7]   SOLUBILITY OF METHANE IN HEAVY NORMAL PARAFFINS AT TEMPERATURES FROM 323-K TO 423-K AND PRESSURES TO 10.7-MPA [J].
DARWISH, NA ;
FATHIKALAJAHI, J ;
GASEM, KAM ;
ROBINSON, RL .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1993, 38 (01) :44-48
[8]   PHASE-EQUILIBRIA IN BINARY-MIXTURES OF ETHANE AND HEXADECANE [J].
DEGOEDE, R ;
PETERS, CJ ;
VANDERKOOI, HJ ;
LICHTENTHALER, RN .
FLUID PHASE EQUILIBRIA, 1989, 50 (03) :305-314
[9]   THE EXPERIMENTAL-DETERMINATION AND MODELING OF VLE FOR BINARY SUBSYSTEMS OF THE QUATERNARY SYSTEM N2 + CH4 + C4H10 + C14H30 UP TO 1000-BAR AND 440-K [J].
DELEEUW, VV ;
DELOOS, TW ;
KOOIJMAN, HA ;
ARONS, JD .
FLUID PHASE EQUILIBRIA, 1992, 73 (03) :285-321
[10]   HYPERBARIC RESERVOIR FLUIDS - HIGH-PRESSURE PHASE-BEHAVIOR OF ASYMMETRIC METHANE PLUS N-ALKANE SYSTEMS [J].
FLOTER, E ;
DELOOS, TW ;
ARONS, JD .
INTERNATIONAL JOURNAL OF THERMOPHYSICS, 1995, 16 (01) :185-194