HCO-TERNARY: A FORTRAN code for calculating P-V-T-X properties and liquid vapor equilibria of fluids in the system H2O-CO2-CH4

Computers and Geosciences

Volumn 29, Issue 4, 2003, Pages 469-485

  Nieva, David ^a   Barragán, Rosa María ^a  

^a INSTITUTO DE INVESTIGACIONES ELÉCTRICAS   (Mexico)

Author keywords

Equation of state; H2O CO2 CH4 fluids; Vapor liquid equilibria; Volumetric properties

Indexed keywords

BINARY MIXTURES; EQUATIONS OF STATE; FORTRAN (PROGRAMMING LANGUAGE); MATHEMATICAL MODELS; PHASE COMPOSITION; PHASE EQUILIBRIA; PRESSURE EFFECTS; THERMAL EFFECTS;

MOLAR VOLUMES;

GEOCHEMISTRY;

COMPUTER SIMULATION; EQUATION OF STATE; FLUID; MODELING; SOFTWARE; TWO PHASE FLOW;

EID: 0037850977     PISSN: 00983004     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0098-3004(03)00016-5     Document Type: Article

References (32)

1. Arai, Y., Kaminishi, G. I., & Saito, S. (1971). The experimental determination of P-V-T-X relations for the carbon dioxide-nitrogen and the carbon dioxide-methane systems. Journal of Chemical Engineering of Japan, 4 113-122.
2. 2 fluid inclusions by microthermometry. Geochimica et Cosmochimica Acta, 64 1753-1764.
3. Blencoe, J. G., Drummond, S. E., Seitz, J. C., & Nesbit, B. E. (1996). A vibrating-tube densimeter for fluids at high pressures and temperatures. International Journal of Thermophysics, 17 179-190.
4. 2O system: III. A new experimental method for determining liquid-vapor equilibria at high subcritical temperatures. American Mineralogist, 86 1100-1111.
5. Burnham, C. W., Holloway, J. R., & Davis, N. F. (1969). The specific volume of water in the range 1000 to 8900 bars 20 to 900°C. American Journal of Science, 267-A 70-95.
6. Callen, H.B., 1960. Thermodynamics. Wiley, New York, 376pp.
7. Culberson, O. L., & McKetta, J. J. (1952). Phase equilibria in hydrocarbon-water systems III-the solubility of methane in water pressures to 10000 psi. Petroleum Transactions, The American Institute of Mining. Metallurgical & Petroleum Engineers, 192 223-226.
8. Donnelly, H. G., & Katz, D. L. (1954). Phase equilibrium in the carbon dioxide-methane system. Industrial and Engineering Chemistry, 46 511-517.
9. Douslin, D. R., Harrison, R. H., Moore, R. T., & McCullough, J. P. (1964). P-V-T relations of methane. Journal of Chemical Engineering Data, 9 358-363.
10. 2O system: I. Pure systems from 0 to 1000°C and 0 to 8000 bar. Geochimica et Cosmochimica Acta, 56 2605-2617.
11. 2O system: II. Mixtures from 50 to 1000°C and 0 to 1000 bar. Geochimica et Cosmochimica Acta, 56 2619-2631.
12. Duan, Z., Møller, N., & Weare, J. H. (1996). A general equation of state for supercritical fluid mixtures and molecular dynamics simulation of mixture properties. Geochimica et Cosmochimica Acta, 60 1209-1216.
13. Fenghour, A., Wakeham, W. A., & Watson, J. T. (1996). Densities of (water+carbon dioxide) in the temperature range 415K to 700K and pressures up to 35Mpa. Journal of Chemical Thermodynamics, 28 433-446.
14. Joffrion, L. L., & Eubank, P. T. (1989). Compressibility factors, densities and residual thermodynamic properties for methane-water mixtures. Journal of Chemical Engineering Data, 34 215-220.
15. Keenan, J.H., Keyes, F.G., Hill, P.G., Moore, J.G., 1978. Steam Tables. Thermodynamics Properties of Water, Including Vapor, Liquid and Solid Phases. Wiley, New York, 156pp.
16. 2 at elevated temperatures and pressures. American Journal of Science, 252 225-241.
17. Malinin, S. D. (1959). The system water-carbon dioxide at high temperatures and pressures. Geochemistry International, 3 292-306.
18. Olds, R. H., Sage, B. H., & Lacey, W. N. (1942). Phase equilibria in hydrocarbon systems: composition of the dew-point gas of the methane-water system. Industrial and Engineering Chemistry, 34 1223-1227.
19. Olds, R. H., Reamer, H. H., Sage, B. H., & Lacey, W. N. (1943). Phase equilibrium in hydrocarbon systems: volumetric behavior of methane. Industrial Engineering Chemistry, 35 922-924.
20. O'Sullivan, M. J. (1981). A similarity method for geothermal well test analysis. Water Resources Research, 17 390-398.
21. Price, L. C. (1979). Aqueous solubility of methane at elevated temperatures and pressures. American Association of Petroleum Geologists Bulletin, 632 1527-1533.
22. 4-bearing fluids in a wolframite vein: reconstruction from fluid inclusion studies. Geochimica et Cosmochimica Acta, 49 205-219.
23. Reamer, H. H., Olds, R. H., Sage, B. H., & Lacey, W. N. (1944). Phase equilibria in hydrocarbon systems: methane-carbon dioxide system in the gaseous region. Industrial Engineering Chemistry, 36 88-90.
24. Roedder, E.R., 1984. Fluid inclusions. Reviews in Mineralogy, Mineralogical Society of America, 12, 644pp.
25. 2 mixtures at 300-400°C and 75-1000 Bars. Proceedings of the Fifth International Symposium on Hydrothermal Reactions, Oak Ridge National Laboratory, Oak Ridge, TN, pp. 109-112.
26. 2O system. I. Experimental determination of volumetric properties at 400°C, 10-100MPa. Geochimica et Cosmochimica Acta, 63 1559-1569.
27. Sultanov, R. G., Skripka, V. G., & Namiot, A. (1971). Moisture content of methane at high temperatures and pressures. Cazovaia Promyshlennost, 16 6-8.
28. 2O at high temperatures and pressures. American Journal of Science, 261 1055-1074.
29. Tödheide K. & Franck, E. U. (1963). Das zweiphasengebiet und die kritische kurve im system kohlendioxid-wasser bis zu drucken von 3500 bar. Zeitschrift für Physikalische Chemie (neue Folge) 37 387-401.
30. 2. Teploenergetika, 10 85-88.
31. 2 density at temperatures from 0 to 35°C and pressures up to 300 bar. Thermal Engineering, 15 103-106.
32. 2 system at 300 and 400°C. Geochemistry International, 21 13-20.