High-pressure vapor-liquid equilibria in the nitrogen-n-pentane system

被引:29
|
作者
Silva-Oliver, Guadalupe
Eliosa-Jimenez, Gaudencio
Garcia-Sanchez, Fernando
Avendano-Gomez, Juan R.
机构
[1] Inst Mexicano Petr, Programa Ingn Mol, Lab Termodinam, Mexico City 07730, DF, Mexico
[2] Inst Politecn Nacl, Unidad Prof Adolfo Lopez Mateos, Lab Invest Ingn Quim Ambiental, SEPI ESIQIE, Mexico City 07738, DF, Mexico
关键词
vapor-liquid equilibria; enhanced oil recovery; equation of state; stability analysis; phase envelope; critical point;
D O I
10.1016/j.fluid.2006.09.018
中图分类号
O414.1 [热力学];
学科分类号
摘要
New experimental vapor-liquid equilibrium data of the N-2-n-pentane system were measured over a wide temperature range from 344.3 to 447.9 K and pressures up to 35 MPa. A static-analytic apparatus with visual sapphire windows and pneumatic capillary samplers was used in the experimental measurements. Equilibrium phase compositions and vapor-liquid equilibrium ratios are reported. The new results were compared with those reported by other authors. The comparison showed that the pressure-composition data reported in this work are in good agreement with those determined by others but they are closer to the mixture critical point at each temperature level. The experimental data were modeled with the PR and PC-SAFF equations of state by using one-fluid mixing rules and a single temperature independent interaction parameter. Results of the modeling showed that the PC-SAFT equation fit the data satisfactorily even at the highest temperatures of study. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:37 / 48
页数:12
相关论文
共 50 条
  • [1] High-pressure vapor-liquid equilibria in the nitrogen-n-nonane system
    Silva-Oliver, Guadalupe
    Eliosa-Jimenez, Gaudencio
    Garcia-Sanchez, Fernando
    Avendano-Gomez, Juan Ramon
    JOURNAL OF SUPERCRITICAL FLUIDS, 2007, 42 (01): : 36 - 47
  • [2] High-pressure vapor-liquid equilibria in the nitrogen plus n-hexane system
    Eliosa-Jimenez, Gaudencio
    Silva-Oliver, Guadalupe
    Garcia-Sanchez, Fernando
    de la Torre, Antonio de Ita
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2007, 52 (02): : 395 - 404
  • [3] HIGH-PRESSURE VAPOR-LIQUID EQUILIBRIA IN AMMONIA-WATER-NITROGEN-HYDROGEN SYSTEM
    GUERRERI, G
    AICHE JOURNAL, 1967, 13 (05) : 877 - &
  • [4] CALCULATION OF HIGH-PRESSURE VAPOR-LIQUID EQUILIBRIA
    CHUEH, PL
    PRAUSNIT.JM
    INDUSTRIAL AND ENGINEERING CHEMISTRY, 1968, 60 (03): : 34 - &
  • [5] High-pressure (vapor plus liquid) equilibria in the (nitrogen plus n-heptane) system
    Garcia-Sanchez, Fernando
    Eliosa-Jimenez, Gaudencio
    Silva-Oliver, Guadalupe
    Godinez-Silva, Armando
    JOURNAL OF CHEMICAL THERMODYNAMICS, 2007, 39 (06): : 893 - 905
  • [6] High-pressure vapor-liquid and vapor-liquid-liquid equilibria in the carbon dioxide+1-heptanol system
    Secuianu, Catinca
    Feroiu, Viorel
    Geana, Dan
    FLUID PHASE EQUILIBRIA, 2008, 270 (1-2) : 109 - 115
  • [7] High-pressure vapor-liquid equilibrium for nitrogen plus methanol
    Laursen, T
    Andersen, SI
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2002, 47 (05): : 1173 - 1174
  • [8] High-pressure vapor-liquid equilibria for carbon dioxide plus limonene
    Iwai, Y
    Morotomi, T
    Sakamoto, K
    Koga, Y
    Arai, Y
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1996, 41 (05): : 951 - 952
  • [9] CALCULATION OF HIGH PRESSURE VAPOR-LIQUID EQUILIBRIA
    CHUEH, PL
    PRAUSNIT.JM
    INDUSTRIAL AND ENGINEERING CHEMISTRY, 1967, 59 (05): : 14 - &
  • [10] Isothermal vapor-liquid equilibria for ethanol and n-pentane system at the near critical region
    Seo, J
    Lee, J
    Kim, H
    FLUID PHASE EQUILIBRIA, 2000, 172 (02) : 211 - 219