Adenekan, A. E., Patzek, T.W. and Pruess, K.: 1993, Modeling of multiphase transport of multicomponent organic contaminants and heat in the subsurface: numerical model formulation, Water Resour. Res.
, 3727–3740.Google Scholar
Anderson, G., Probst, A., Murray, L. and Butler, S.: 1992, An accurate PVT model for geothermal fluids as represented by H2O-CO2-NaCl mixtures, Proc. 17th Workshop on Geothermal Reservoir Engineering, Stanford University, January 1992.
Corey, A. T.: 1977, Mechanics of Heterogeneous Fluids in Porous Media
, Water Resources Publications, Fort Collins, USA.Google Scholar
de Santis, R., Gironi, F. and Marrelli, L.: 1976, Vapor-liquid equilibrium from a hard-sphere equation of state. Ind. End. Chem. Fundam.
, 183–189.Google Scholar
Duan, Z., Moller, N. and Wear, J. H.: 1992, An equation of state for the system CH4-CO2-H2O system: I. Pure systems from 0 to 1000° and 0 to 8000 bar.
Duan, Z., Moller, N. and Wear, J. H.: 1992, An equation of state for the system CH4-CO2-H2O system: II. Mixtures from 50 to 1000° and 0 to 8000 bar.
Fuller, G. G.: 1976, A modified Redlich-Kwong equation of state capable of representing the liquid state, Ind. Eng. Chem. Fundam.
, 254–257.Google Scholar
Hendriks, C. S. and Blok, K.: 1994, Costs of underground storage of carbon dioxide, ICCDR-2, Kyoto, October 1994.
Hirschfelder, J. O. and Curtiss, C. F.: 1954, Molecular Theory of Gases
, Wiley, New York.Google Scholar
Hort, T., Jensen, J. and Lindeberg, E.: 1995, Underground storage of CO2 in aquifers and oil reservoirs. Proceedings of the Second International Conference on Carbon Dioxide Removal, Kyoto, Japan, 24–27 October, 1994.
Kerrick, D. M. and Jacobs, G. K.: 1981, A modified Redlich-Kwong equation for H2O,CO2 and H2O-CO2 mixtures at elevated pressures and temperatures, Amer. J. Sci.
Kondo, J., Inui, T. and Wasa, K.: 1994, Proceedings of the second international conference on carbon dioxide removal, Energy Conversion and Management
, 6–9.Google Scholar
Korbol, R.: 1995, Sleipner Vest CO2 Disposal: Injection of extracted CO2 into the Utsira formation, Proceedings of the Second International Conference on Carbon Dioxide Removal, Kyoto, Japan, 24–27 October, 1994.
L'vovich, M. I.: 1979, World Water Resources and their Future, AGU Translation Board (Publisher), 15.
Ohgaki, K., Makihara, Y. and Tokano, K.: 1993, Formation of CO2
hydrate in pure and sea waters, J. Chem. Eng. Japan
(6), 554–564.Google Scholar
Ohgaki, K. and Akano, T.: 1992, Energy and Resources
(in Japanese) 13
, 375–383.Google Scholar
O'Sullivan, M. J., Bodvarsson, G. S., Pruess, K. and Blakeley, M. R.: 1985, Fluid and heat flow in gas-rich geothermal reservoirs, Soc. Pet. Eng. J.
, 215–225.Google Scholar
Patel, M. R. and Eubank, P. T.: 1988, Experimental densities and derived thermodynamic properties for carbon dioxide-water mixtures, J. Chem. Eng. Data
, 185–193.Google Scholar
Peng, D. and Robinson, D. B.: 1976, A new two-constant equation of state, Ind. Eng. Chem. Fundamentals
, 59–64.Google Scholar
Prausnitz, J. M.: 1969, Molecular Thermodynamics of Fluid-Phase Equilibria
, Prentice-Hall Inc., Englewood Cliffs, New Jersey, p. 41.Google Scholar
Pruess, K.: 1987, Tough user's guide, Report NUREG/CR-4645, Nucl. Reg. Comm., Washington, D.C.Google Scholar
Pruess, K.: 1991, TOUGH2 - A General-purpose numerical simulator for multiphase fluid and heat flow, Report LBL-29400, Lawrence Berkeley Laboratory.
Redlich, O. and Kwong, J. N. S.: 1949, On the thermodynamics of solutions V. An equation of state. Fugacities of gaseous solutions, Chem. Rev.
, 233–244.Google Scholar
Sarmiento, J. L.: 1993, Nature
, 697–698.Google Scholar
Soave, G.: 1972, Equilibrium constants from a modified Redlich-Kwong equation of state, Chem. Eng. Sci.
, 1197–1203.Google Scholar
Steinberg, M., Cheng, H. C. and Horn, F.: 1995, A system study for the removal, recovery and disposal of carbon dioxide from fossil fuel plants in the US, Brookhaven National Laboratory.
Sweigert, R. L., Weber, P. and Allen, R. L.: 1946, Thermodynamic properties of gases: carbon dioxide, Ind. Eng. Chem.
Takenouchi, G. C. and Kennedy, G. C.: 1964, The binary system H2O-CO2 at high temperatures and pressures, Amer. J. Sci.
UK Steam Tables in SI Units: 1970, Edward Arnold, London.
Vesovic, V., Wakeham, W. A., Olchowy, G. A., Sengers, J. V., Watson, J. T. R. and Millat, J: 1990, The transport properties of carbon dioxide, J. Phys. Chem. Ref. Data
Zawisza, A. and Malesinska, B.: 1981, Solubility of carbon dioxide in liquid water and of water in gaseous carbon dioxide in the range 0.2–5 Mpa and at temperatures up to 473°K, J. Chem. Eng. Data
, 388–391.Google Scholar