Extension of the E-PPR78 equation of state to predict fluid phase equilibria of natural gases containing carbon monoxide, helium-4 and argon

被引:29
作者
Plee, Vincent [1 ]
Jaubert, Jean-Noel [1 ]
Privat, Romain [1 ]
Arpentinier, Philippe [2 ]
机构
[1] Univ Lorraine, Ecole Natl Super Ind Chim, Lab React & Genie Proc, UMR CNRS 7274, F-54000 Nancy, France
[2] Ctr Rech Paris Saclay, Air Liquide, F-78354 Jouy En Josas, France
关键词
E-PPR78; predictive equation of state; Peng-Robinson; natural gas; LIQUID-VAPOR-EQUILIBRIUM; PENG-ROBINSON EOS; BINARY INTERACTION PARAMETERS; 2ND VIRIAL-COEFFICIENTS; EXCESS THERMODYNAMIC PROPERTIES; HEAVY NORMAL-PARAFFINS; SULFHYDRYL-GROUP SH; PPR78; MODEL; SUPERCRITICAL CO2; LOW-TEMPERATURES;
D O I
10.1016/j.petrol.2015.03.025
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The E-PPR78 model is a predictive version of the widely used Peng-Robinson equation of state in which the binary interaction parameters are estimated by a group-contribution method. With the 21 groups available before the writing of this paper, such a model could be used to predict fluid phase equilibria of systems containing hydrocarbons, permanent gases (CO2, N-2, H2S, H-2), mercaptans, alkenes and water. In other words, all the components encountered in petroleum fluids could be modeled. It is however acknowledged that natural gases often contain small amounts of carbon monoxide, helium or argon. In order to model the phase behavior and estimate energetic properties (e.g. enthalpy changes on mixing) of such gases, the applicability range of the E-PPR78 model is extended through the addition of three new groups: CO, He and Ar. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:744 / 770
页数:27
相关论文
共 196 条
  • [1] Natural gas to synthesis gas - Catalysts and catalytic processes
    Aasberg-Petersen, K.
    Dybkjaer, I.
    Ovesen, C. V.
    Schjodt, N. C.
    Sehested, J.
    Thomsen, S. G.
    [J]. JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2011, 3 (02) : 423 - 459
  • [2] EXCESS PROPERTIES OF (ETHANE + PROPANE) (L) AND (CARBON-MONOXIDE + METHANE) (L)
    ADAMS, WR
    GOPAL, P
    ZOLLWEG, JA
    STREETT, WB
    [J]. JOURNAL OF CHEMICAL THERMODYNAMICS, 1987, 19 (01) : 39 - 46
  • [3] Akers W., 1957, ADV CRYOGEN ENGNG, V3, P275
  • [4] Calculation of phase equilibrium of natural gases with the Peng-Robinson and PC-SAFT equations of state
    Alfradique, M. F.
    Castier, M.
    [J]. OIL & GAS SCIENCE AND TECHNOLOGY-REVUE D IFP ENERGIES NOUVELLES, 2007, 62 (05): : 707 - 714
  • [5] [Anonymous], 2006, 122131 ISO 1
  • [6] Thermodynamic properties of light synthetic natural gas mixtures using the RK-PR cubic equation of state
    Aparicio Martinez, Santiago
    Hall, Kenneth R.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (10) : 3684 - 3692
  • [7] Aronovich R., 1988, NEFTEKHIMIYA, V28, P670
  • [8] Arpentinier P., 2014, COMMUNICATION
  • [9] Augood D., 1957, Trans. Inst. Chem. Eng, V35, P394
  • [10] Thermodynamic modeling for petroleum fluids - I. Equation of state and group contribution for the estimation of thermodynamic parameters of heavy hydrocarbons
    Avaullee, L
    Trassy, L
    Neau, E
    Jaubert, JN
    [J]. FLUID PHASE EQUILIBRIA, 1997, 139 (1-2) : 155 - 170