Experimental and Molecular Modeling Study of the Three-Phase Behavior of (n-Decane plus Carbon Dioxide plus Water) at Reservoir Conditions

被引:32
|
作者
Forte, Esther [1 ]
Galindo, Amparo [1 ]
Trusler, J. P. Martin [1 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn, London SW7 2AZ, England
来源
JOURNAL OF PHYSICAL CHEMISTRY B | 2011年 / 115卷 / 49期
基金
英国工程与自然科学研究理事会;
关键词
EQUATION-OF-STATE; VAPOR-LIQUID-EQUILIBRIA; ASSOCIATING FLUID THEORY; SAFT-VR APPROACH; DIRECTIONAL ATTRACTIVE FORCES; THERMODYNAMIC PERTURBATION-THEORY; PHASE-EQUILIBRIA; HIGH-PRESSURE; MUTUAL SOLUBILITIES; BINARY-MIXTURES;
D O I
10.1021/jp206806a
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Knowledge of the phase behavior of mixtures of oil with carbon processes of enhanced oil recovery and geological storage of carbon dioxide However, for a comprehensive understanding, the study of simpler systems dioxide and water is essential for reservoir engineering, especially in the needs to be completed. In this Work the system (n-decane + carbon dioxide + water), was studied as a model (oil + Carbon oxide + water) mixture. To high pressure was designed with maximum operating temperature and pressure. of 423 K and 45 MPa, respectively. The equipment relies on recirculation of two coexisting phases using a two-channel magnetically operated rnicropump designed. during this work, with sampling and online compositional analysis. by gas Chromatography. The apparatus has been validated by comparison with published isothermal vapor liquid equilibrium data for the binary system (n-decane + carbon dioxide). New experimental data have been measured for the system (n-decane + carbon dioxide + water) under conditions of three-phase equilibria. Data for the three coexisting phases have been obtained on five isotherms at temperatures from 323 to 413 K and at pressures up to the point at which two of the phases become critical. The experimental work is complemented here with a theoretical effort in which we developed models for these molecules within the framework of the statistical associating fluid theory for potentials of variable range (SAFT-VR). The phase behavior of the three binary subsystems was calculated using this theory, and Where applicable, a modification of the Hudson and McCoubrey combining rules was used to treat the systems predictively. The experimental data obtained for the ternary mixture are compared to the predictions of the theory. Furthermore, a detailed analysis of the ternary mixture is carried out based on comparison with available data for the constituent binary subsystems. In this way, we analyzed the observed effects on the solubility when the third component was added.
引用
收藏
页码:14591 / 14609
页数:19
相关论文
共 50 条
  • [31] High-pressure phase behavior of the quaternary system (carbon dioxide plus dichloromethane plus ε-caprolactone plus poly(ε-caprolactone): Experimental data and PC-SAFT modeling
    Santos, Nilson G. O.
    Rebelatto, Evertan A.
    Mayer, Diego A.
    Lanza, Marcelo
    Oliveira, J. Vladimir
    [J]. FLUID PHASE EQUILIBRIA, 2022, 554
  • [32] On the phase behaviour of the (carbon dioxide plus water) systems at low temperatures: Experimental and modelling
    Chapoy, Antonin
    Haghighi, Hooman
    Burgass, Rod
    Tohidi, Bahman
    [J]. JOURNAL OF CHEMICAL THERMODYNAMICS, 2012, 47 : 6 - 12
  • [33] Measurement and correlation of high pressure phase behavior of carbon dioxide plus water system
    Han, Ji Min
    Shin, Hun Yong
    Min, Byoung-Moo
    Han, Keun-Hee
    Cho, Ara
    [J]. JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2009, 15 (02) : 212 - 216
  • [34] Phase behavior of the poly(vinyl pyrrolidone) plus N-vinyl-2-pyrrolidone plus carbon dioxide system
    Bae, W
    Kwon, SY
    Byun, HS
    Kim, HY
    [J]. JOURNAL OF SUPERCRITICAL FLUIDS, 2004, 30 (02): : 127 - 137
  • [35] Phase Behavior of the System (Carbon Dioxide plus n-Heptane plus Methylbenzene): A Comparison between Experimental Data and SAFT-γ-Mie Predictions
    Al Ghafri, Saif Z. S.
    Maitland, Geoffrey C.
    Trusler, J. P. Martin
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2017, 62 (09): : 2826 - 2836
  • [36] Understanding the Phase Behavior of Tetrahydrofuran plus Carbon Dioxide, plus Methane, and plus Water Binary Mixtures from the SAFT-VR Approach
    Miguez, J. M.
    Pineiro, M. M.
    Algaba, J.
    Mendiboure, B.
    Torre, J. P.
    Blas, F. J.
    [J]. JOURNAL OF PHYSICAL CHEMISTRY B, 2015, 119 (44): : 14288 - 14302
  • [37] Measurement and modeling of the phase behavior of the (carbon dioxide plus water) mixture at temperatures from 298.15 K to 448.15 K
    Hou, Shu-Xin
    Maitland, Geoffrey C.
    Trusler, J. P. Martin
    [J]. JOURNAL OF SUPERCRITICAL FLUIDS, 2013, 73 : 87 - 96
  • [38] Microscopic phase behavior of supercritical carbon dioxide plus non-ionic surfactant plus water systems at elevated pressures
    Haruki, Masashi
    Matsuura, Kazuhiko
    Kaida, Yuichi
    Kihara, Shin-ichi
    Takishima, Shigeki
    [J]. FLUID PHASE EQUILIBRIA, 2010, 289 (01) : 1 - 5
  • [39] Study of Gas Hydrate Formation in the Carbon Dioxide plus Hydrogen plus Water Systems: Compositional Analysis of the Gas Phase
    Belandria, Veronica
    Eslamimanesh, Ali
    Mohammadi, Amir H.
    Richon, Dominique
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (10) : 6455 - 6459
  • [40] Simulation and measurements of volumetric and phase behavior of carbon dioxide plus higher alkanes at high pressure: CO2 + n-decane at temperatures (313-410) K and pressures up to 76MPa
    Kandil, Mohamed E.
    Al-Saifi, Nayef M.
    Sultan, Abdullah S.
    [J]. INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2016, 53 : 198 - 206