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

被引:19
|
作者
Kandil, Mohamed E. [1 ]
Al-Saifi, Nayef M. [2 ]
Sultan, Abdullah S. [1 ]
机构
[1] King Fahd Univ Petr & Minerals, Coll Petr Engn & Geosci, Dhahran 31261, Saudi Arabia
[2] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran 31261, Saudi Arabia
关键词
Carbon dioxide; Decane; CO2-EOR; Higher alkanes; Phase behavior; Density; Bubble pressure; PVT; EQUATION-OF-STATE; VIBRATING-WIRE VISCOMETER; CENTER-DOT-S; T=298 K; THERMODYNAMIC PROPERTIES; INTERFACIAL-TENSIONS; PERTURBATION-THEORY; NOMINAL VISCOSITY; REFERENCE FLUID; P=0.1 MPA;
D O I
10.1016/j.ijggc.2016.07.045
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Injection of CO2 in hydrocarbon rock formation is one of the proven technologies for both enhanced oil recovery and carbon sequestration. Accurate knowledge of thermodynamic properties of CO2 and reservoir fluid mixtures are required for successful design and operation. In this work, new rho Tp and bubble pressure p(b) measurements are reported for the binary system of carbon dioxide (1) + n-decane (2). Compressed liquid density was determined from the complex resonance frequency of a vibrating U-tube driven by a lock-in amplifier and bubble points were visually detected and also calculated from the discontinuity of a p-V plot of a constant composition isothermal expansion process (CCE). The measurements were made along three isotherms at temperatures T=(313, 363, and 410) K at pressures up to 76MPa for three concentrations of carbon dioxide mole fraction x(1) = (0.207, 0.471, and 0.730). The experimental results are compared with previous experimental data in literature, and with predictions from four types of equations of state (EOS), commonly used in petroleum and chemical industry: (1) cubic, Peng-Robinson (PR); (2) virial, Benedict-Webb-Rubin Starling (BWRS); multi-parameters, Groupe European de Recherche Gaziere (GERG-2008); and (4) Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT). Analysis of all experimental data, in previous literature and this work, show a systematic increase in deviations from both BWRS and PC-SAFT from 1% to about 10% with increasing carbon dioxide mole fraction which is a clear evidence of the need for adjusting the equation's parameters, especially at pressures close to bubble points. Best prediction for density was obtained with GERG-2008 EOS, with deviations of about 1%, for all CO2 mole fractions from (0.05 to 0.87), and best prediction for phase behavior was obtained by PR EOS. Earlier experimental data are only limited to 40 MPa, while this work extends the measurements to a higher range, of 76 MPa and 410 K, commonly encountered in gas reservoirs and supercritical CO2 injection processes, and not studied before. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:198 / 206
页数:9
相关论文
共 18 条
  • [1] Measurements and Modeling of Volumetric and Phase Behavior of Carbon Dioxide plus Higher Alkanes: CO2 + n-Pentadecane at Temperatures 313 to 410 K and Pressures up to 77 MPa
    Kandil, Mohamed E.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2018, 63 (05): : 1389 - 1396
  • [2] Measurements and Modeling of Phase Behavior, Density, and Viscosity of Oil plus Carbon Dioxide: Squalane + CO2 at Temperatures (313 to 363) K and Pressures up to 77 MPa
    Kandil, Mohamed E.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2019, 64 (01): : 273 - 285
  • [3] Density and Volumetric Behavior of Binary CO2 + n-Decane and Ternary CO2 + n-Decane plus Naphthalene Systems at High Pressure and High Temperature
    Chacon Valero, Angelica Maria
    Feitosa, Filipe Xavier
    de Sant'Ana, Hosiberto Batista
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2020, 65 (07): : 3499 - 3509
  • [4] Density and Volumetric Behavior of Ternary CO2 + n-Decane plus n-Butylcyclohexane Mixtures at High Pressure and High Temperature
    Chacon Valero, Angelica Maria
    Alves, Caiua Araujo
    Gomes de Medeiros, Peterson Yamagushi
    Feitosa, Filipe Xavier
    de Sant'Ana, Hosiberto Batista
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2022, 67 (06): : 1397 - 1405
  • [5] Density and Volumetric Behavior of Ternary CO2 + n-Decane plus cis-Decalin (or plus trans-Decalin) Mixtures at High Pressure and High Temperature
    Chacon Valero, Angelica Maria
    Alves, Caiva Aranjo
    Feitosa, Filipe Xavier
    de Sant'Ana, Hosiberto Batista
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2021, 66 (04): : 1684 - 1693
  • [6] Phase behavior of (CO2 + H2) and (CO2+ N2) at temperatures between (218.15 and 303.15)K at pressures up to 15 MPa
    Fandino, Olivia
    Trusler, J. P. Martin
    Vega-Maza, David
    INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2015, 36 : 78 - 92
  • [7] HIGH-PRESSURE VAPOR-LIQUID-EQUILIBRIA FOR CO2 PLUS BENZONITRILE, CO2 PLUS BENZYL ALCOHOL, CO2 PLUS 2-TERT-BUTYLPHENOL, CO2 PLUS METHOXYBENZENE, AND CO2 PLUS 1,2,3,4-TETRAHYDRONAPHTHALENE AT TEMPERATURES BETWEEN 313 AND 393 K AND PRESSURES UP TO 20 MPA
    WALTHER, D
    MAURER, G
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1993, 38 (02): : 247 - 249
  • [8] Liquid and Dense Phase Thermal Conductivity Measurements of CO2 + N2 and CO2 + CH4 Mixtures at Temperatures from 223 K to 308 K and Pressures up to 20 MPa
    Kim, Dongchan
    Lovseth, Sigurd Weidemann
    Arami-Niya, Arash
    May, Eric F.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2021, 66 (11): : 4018 - 4029
  • [9] Measurements of compressed liquid densities for CO2 (1) plus butan-1-ol (2) via a vibrating tube densimeter at temperatures from (313 to 363) K and pressures up to 25 MPa
    Zuniga-Moreno, Abel
    Galicia-Luna, Luis A.
    Sandler, Stanley I.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2007, 52 (05): : 1960 - 1969
  • [10] Isothermal vapor-liquid equilibria of the carbon dioxide (CO2)-N,N-dimethylformamide (DMF) system at temperatures from 293.95 K to 338.05 K and pressures up to 12 MPa
    Duran-Valencia, C
    Valtz, A
    Galicia-Luna, LA
    Richon, D
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2001, 46 (06): : 1589 - 1592