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Volumn 67, Issue , 2012, Pages 41-52

Prediction of multicomponent phase behavior of CO 2-expanded liquids using CEoS/GE models and comparison with experimental data

Author keywords

CEoS GE; CO 2 expanded liquids; Experimental VLE data; Hydroformylation; Phase behavior; VLE

Indexed keywords

1-OCTENE; CEOS/GE; CUBIC EQUATION OF STATE; EXPANDED LIQUID; EXPERIMENTAL DATA; MIXING RULES; MODEL DISCRIMINATION; MODELING APPROACH; MULTICOMPONENTS; OPERATING CONDITION; OPTIMAL PERFORMANCE; PREDICTIVE CAPABILITIES; QUATERNARY SYSTEMS; QUINARY SYSTEM; SEPARATION UNITS; SUB-SYSTEMS; VLE; VLE DATA;

EID: 84862114270     PISSN: 08968446     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.supflu.2012.03.007     Document Type: Article
Times cited : (12)

References (32)
  • 3
    • 33644915590 scopus 로고    scopus 로고
    • 2+ toluene from 305 to 343 K and 1.2 to 10.5 MPa
    • 2+ toluene from 305 to 343 K and 1.2 to 10.5 MPa Fluid Phase Equilibria 242 2006 111 117
    • (2006) Fluid Phase Equilibria , vol.242 , pp. 111-117
    • Yin, J.Z.1    Tan, C.S.2
  • 8
    • 12344255099 scopus 로고    scopus 로고
    • Vapor-liquid equilibria of the carbon dioxide plus acetone system at pressures from (2.36 to 11.77) MPa and temperatures from (333.15-393.15) K
    • F. Han, Y. Xue, Y.L. Tian, X.F. Zhao, and L. Chen Vapor-liquid equilibria of the carbon dioxide plus acetone system at pressures from (2.36 to 11.77) MPa and temperatures from (333.15-393.15) K Journal of Chemical & Engineering Data 50 2005 36 39
    • (2005) Journal of Chemical & Engineering Data , vol.50 , pp. 36-39
    • Han, F.1    Xue, Y.2    Tian, Y.L.3    Zhao, X.F.4    Chen, L.5
  • 10
    • 55349104802 scopus 로고    scopus 로고
    • Vapor-liquid phase boundaries of binary mixtures of carbon dioxide with ethanol and acetone
    • H.Y. Chin, M.J. Lee, and H.M. Lin Vapor-liquid phase boundaries of binary mixtures of carbon dioxide with ethanol and acetone Journal of Chemical & Engineering Data 53 2008 2393 2402
    • (2008) Journal of Chemical & Engineering Data , vol.53 , pp. 2393-2402
    • Chin, H.Y.1    Lee, M.J.2    Lin, H.M.3
  • 13
    • 84927489296 scopus 로고
    • Direct determination of fluid-phase equilibria by simulation in the gibbs ensemble - A review
    • A.Z. Panagiotopoulos Direct determination of fluid-phase equilibria by simulation in the gibbs ensemble - a review Molecular Simulation 9 1992 1 23
    • (1992) Molecular Simulation , vol.9 , pp. 1-23
    • Panagiotopoulos, A.Z.1
  • 14
    • 34548304724 scopus 로고    scopus 로고
    • Prediction of phase equilibria and transport properties in carbon-dioxide expanded solvents by molecular simulation
    • Y. Houndonougbo, K. Kuczera, B. Subramaniam, and B.B. Laird Prediction of phase equilibria and transport properties in carbon-dioxide expanded solvents by molecular simulation Molecular Simulation 33 2007 861 869
    • (2007) Molecular Simulation , vol.33 , pp. 861-869
    • Houndonougbo, Y.1    Kuczera, K.2    Subramaniam, B.3    Laird, B.B.4
  • 17
    • 78650190191 scopus 로고    scopus 로고
    • Aspen Technology, Inc.
    • Aspen Plus V7.1, Aspen Technology, Inc.
    • Aspen Plus V7.1
  • 18
    • 0026867521 scopus 로고
    • A theoretically correct mixing rule for cubic equations of state
    • D.S.H. Wong, and S.I. Sandler A theoretically correct mixing rule for cubic equations of state AIChE Journal 38 1992 671 680
    • (1992) AIChE Journal , vol.38 , pp. 671-680
    • Wong, D.S.H.1    Sandler, S.I.2
  • 20
    • 0031377968 scopus 로고    scopus 로고
    • Prediction of vapor-liquid equilibria with the LCVM model: Systems containing light gases with medium and high molecular weight compounds
    • C.J. Boukouvalas, K.G. Magoulas, S.K. Stamataki, and D.P. Tassios Prediction of vapor-liquid equilibria with the LCVM model: systems containing light gases with medium and high molecular weight compounds Industrial and Engineering Chemistry Research 36 1997 5454 5460
    • (1997) Industrial and Engineering Chemistry Research , vol.36 , pp. 5454-5460
    • Boukouvalas, C.J.1    Magoulas, K.G.2    Stamataki, S.K.3    Tassios, D.P.4
  • 21
    • 11844284026 scopus 로고    scopus 로고
    • PSRK group contribution equation of state: Comprehensive revision and extension IV, including critical constants and alpha-function parameters for 1000 components
    • S. Horstmann, A. Jabloniec, J. Krafczyk, K. Fischer, and J. Gmehling PSRK group contribution equation of state: comprehensive revision and extension IV, including critical constants and alpha-function parameters for 1000 components Fluid Phase Equilibria 227 2005 157 164
    • (2005) Fluid Phase Equilibria , vol.227 , pp. 157-164
    • Horstmann, S.1    Jabloniec, A.2    Krafczyk, J.3    Fischer, K.4    Gmehling, J.5
  • 22
    • 0018544434 scopus 로고
    • New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures
    • M.J. Huron, and J. Vidal New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures Fluid Phase Equilibria 3 1979 255 271
    • (1979) Fluid Phase Equilibria , vol.3 , pp. 255-271
    • Huron, M.J.1    Vidal, J.2
  • 23
    • 0029386662 scopus 로고
    • On the combination of equation of state and excess free-energy models
    • H. Orbey, and S.I. Sandler On the combination of equation of state and excess free-energy models Fluid Phase Equilibria 111 1995 53 70
    • (1995) Fluid Phase Equilibria , vol.111 , pp. 53-70
    • Orbey, H.1    Sandler, S.I.2
  • 24
    • 0032208679 scopus 로고    scopus 로고
    • Connection between zero-pressure mixing rules and infinite-pressure mixing rules
    • C.H. Twu, J.E. Coon, D. Bluck, B. Tilton, and M. Rowland Connection between zero-pressure mixing rules and infinite-pressure mixing rules Fluid Phase Equilibria 153 1998 29 44
    • (1998) Fluid Phase Equilibria , vol.153 , pp. 29-44
    • Twu, C.H.1    Coon, J.E.2    Bluck, D.3    Tilton, B.4    Rowland, M.5
  • 25
    • 0025499797 scopus 로고
    • A method for incorporating excess Gibbs energy models in equations of state
    • M.L. Michelsen A method for incorporating excess Gibbs energy models in equations of state Fluid Phase Equilibria 60 1990 47 58
    • (1990) Fluid Phase Equilibria , vol.60 , pp. 47-58
    • Michelsen, M.L.1
  • 26
    • 0025499090 scopus 로고
    • A modified huron-vidal mixing rule for cubic equations of state
    • M.L. Michelsen A modified huron-vidal mixing rule for cubic equations of state Fluid Phase Equilibria 60 1990 213 219
    • (1990) Fluid Phase Equilibria , vol.60 , pp. 213-219
    • Michelsen, M.L.1
  • 27
    • 0025555405 scopus 로고
    • High-pressure vapor-liquid equilibrium with a UNIFAC-based equation of state
    • S. Dahl, and M.L. Michelsen High-pressure vapor-liquid equilibrium with a UNIFAC-based equation of state AIChE Journal 36 1990 1829 1836
    • (1990) AIChE Journal , vol.36 , pp. 1829-1836
    • Dahl, S.1    Michelsen, M.L.2
  • 28
    • 0027625166 scopus 로고
    • Prediction of vapor-liquid-equilibria at high-pressures using activity-coefficient parameters obtained from low-pressure data - A comparison of 2 equation of state mixing rules
    • H. Huang, and S.I. Sandler Prediction of vapor-liquid-equilibria at high-pressures using activity-coefficient parameters obtained from low-pressure data - a comparison of 2 equation of state mixing rules Industrial and Engineering Chemistry Research 32 1993 1498 1503
    • (1993) Industrial and Engineering Chemistry Research , vol.32 , pp. 1498-1503
    • Huang, H.1    Sandler, S.I.2
  • 29
    • 0026831748 scopus 로고
    • A new expression of Q(Alpha) for the modified huron-vidal method
    • G. Soave A new expression of Q(Alpha) for the modified huron-vidal method Fluid Phase Equilibria 72 1992 325 327
    • (1992) Fluid Phase Equilibria , vol.72 , pp. 325-327
    • Soave, G.1
  • 30
    • 0031148512 scopus 로고    scopus 로고
    • A comparison of huron-vidal type mixing rules of mixtures of compounds with large size differences, and a new mixing rule
    • H. Orbey, and S.I. Sandler A comparison of huron-vidal type mixing rules of mixtures of compounds with large size differences, and a new mixing rule Fluid Phase Equilibria 132 1997 1 14
    • (1997) Fluid Phase Equilibria , vol.132 , pp. 1-14
    • Orbey, H.1    Sandler, S.I.2
  • 31
    • 67849099225 scopus 로고    scopus 로고
    • Prediction of vapor-liquid equilibrium at high pressure using a new excess free energy mixing rule coupled with the original UNIFAC method and the SRK equation of state
    • Z.H. Chen, Z. Yao, Y. Li, K. Cao, and Z.M. Huang Prediction of vapor-liquid equilibrium at high pressure using a new excess free energy mixing rule coupled with the original UNIFAC method and the SRK equation of state Industrial and Engineering Chemistry Research 48 2009 6836 6845
    • (2009) Industrial and Engineering Chemistry Research , vol.48 , pp. 6836-6845
    • Chen, Z.H.1    Yao, Z.2    Li, Y.3    Cao, K.4    Huang, Z.M.5
  • 32
    • 0028173676 scopus 로고
    • Prediction of vapor-liquid-equilibrium with the LCVM model - A linear combination of the vidal and michelsen mixing rules coupled with the original UNIFAC and the T-MPR equation of state
    • C. Boukouvalas, N. Spiliotis, P. Coutsikos, N. Tzouvaras, and D. Tassios Prediction of vapor-liquid-equilibrium with the LCVM model - a linear combination of the vidal and michelsen mixing rules coupled with the original UNIFAC and the T-MPR equation of state Fluid Phase Equilibria 92 1994 75 106
    • (1994) Fluid Phase Equilibria , vol.92 , pp. 75-106
    • Boukouvalas, C.1    Spiliotis, N.2    Coutsikos, P.3    Tzouvaras, N.4    Tassios, D.5


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.