Phase equilibria modeling applied to fluid inclusions: Liquid-vapor equilibria and calculation of the molar volume in the CO[sub 2]-CH[sub 4]-N[sub 2] system
- Centre de Recherche sur la Geologie des Matieres Minerales et Energetiques, Vandoeuvre-les-Nancy (France)
- Laboratoire de thermodynamique, Rueil Malmaison (France)
Quantitative use of fluid inclusions requires the determination of composition and molar volume. The molar volume can be calculated in the CO[sub 2]-CH[sub 4]N[sub 2] system from both the determination of the temperature of a L + V [yields] L (or V) equilibrium if the composition is known independently, provided an equation of state (EOS) reproduces the P-V-T-X properties of each phase at equilibrium. This study is applicable to fluids for which the sequence of phase transition is S[sub CO2] + L + V [yields] L + V [yields] L (or V) at increasing temperature. The molar volume is determined by following a two-step algorithm: (1) the pressure is calculated from a two-parameter cubic EOS with interaction parameters optimized along experimental L-V isotherms (2) the molar volume is then calculated by the correlation of LEE and KESLER (1975) with the pressure calculated in the first step. Projections of polybaric L-V isotherms in [upsilon]-X diagrams of the CO[sub 2]-CH[sub 4], CO[sub 2]-N[sub 2], and CH[sub 4]-N[sub 2] systems can be directly applied to fluid inclusion studies. In addition, it is shown that the molar volume of CO[sub 2]-rich fluids (X[sub CO2] > 0.6) in the ternary system can be estimated with sufficient accuracy using empirical formulae relating to the [upsilon]-X diagrams of the CO[sub 2]-CH[sub 4] and CO[sub 2]-N[sub 2] binary systems.
- OSTI ID:
- 7164911
- Journal Information:
- Geochimica et Cosmochimica Acta; (United States), Vol. 58:3; ISSN 0016-7037
- Country of Publication:
- United States
- Language:
- English
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