(222af) Experimental and Modeling Study of the Phase Behavior of CO2-Hydrocabon-Water Mixtures
Experimental and Modeling Study of
the Phase Behavior of CO2-Hydrocabon-Water Mixtures
Saif Zahir Al Ghafri, Esther
Forte, Amparo Galindo, Geoffrey C. Maitland, and J. P. Martin Trusler*
Qatar Carbonates and Carbon Storage Research Centre,
Department of Chemical Engineering, Imperial College London, South Kensington Campus,
London SW7 2AZ
* Corresponding author e-mail:
Experimental phase-behavior data for
CO2-hydrocarbon-water mixtures play a fundamental role in reservoir
engineering and reservoir management, wherein phase equilibrium data at
reservoir conditions are required for determination of the in-place volume and
recovery factor. These data are also key inputs to reservoir simulations, used
for evaluating reservoir development plans, and are required for the
interpretation of well-test data and in the design of the surface facilities
and processing plants. Knowledge of phase behavior for these mixtures is also
crucial in carbon capture and storage (CCS) and enhanced oil recovery (EOR) processes
where the miscibility of carbon dioxide with hydrocarbons plays an essential
role. Furthermore, measuring
the mutual solubility of water and hydrocarbon fluids and the water content of
hydrocarbon gases and non-hydrocarbon gases such as CO2 is necessary
to assess corrosion problems caused by moisture condensation in pipelines or
process equipment, and to determine the dosage of chemical inhibitor required to
avoid hydrate crystal formation which may block pipelines, equipment and
to the complexity of oil mixtures, simpler systems that may represent certain
characteristics of the real ones are often studied. Despite their importance as
a simple model for reservoir fluids, experimental data for CO2-hydrocarbon-water
ternary mixtures are scarce and limited to VLE measurements in most cases. Although
much effort has been dedicated to the development of integrated modeling approaches
for the prediction of phase behavior and other thermophysical
properties of mixtures, experimental data are still required to tune the
interaction parameters of the models or to assess the predictive capability of
models. Therefore, any new measurements on ternary mixtures of the type CO2
+ hydrocarbon + water is a valuable addition to the literature especially in
the three phase, VLLE, region.
In this work the phase equilibria
of (n-heptane + carbon dioxide + water) and (methane + carbon dioxide + water)
mixtures have been measured. The n-heptane system was chosen as being a
representative model for (light oil fraction + carbon dioxide + water, while
the methane system is considered representative of (natural gas + carbon
dioxide + water). The phase equilibrium measurements were carried out using a high-pressure
quasi-static-analytical apparatus that was previously described previously .
The apparatus relies on recirculation of two coexisting phases using a
two-channel magnetically operated micro-pump with sampling and on-line
compositional analysis by gas chromatography. The maximum operating temperature
and pressure of this apparatus are 423 K and 45 MPa,
respectively. The apparatus was calibrated and validated by means of comparison
with the published available literature data of the systems (n-heptane + carbon
dioxide) and (water + carbon dioxide).
this work, new experimental data have been measured for the system (n-heptane +
carbon dioxide + water) under conditions of three-phase equilibria.
Compositions of the three coexisting phases have been obtained along five
isotherms at temperatures from (323.15 to 413.15) K and at pressures up to an
upper critical end point at which the heptane-rich and the carbon dioxide-rich phases
become critical. In addition, new experimental data have been measured for the
system (methane + carbon dioxide + water) under conditions of two-phase
vapor-liquid equilibrium, three-phase vapor-liquid-liquid equilibrium, and four-phase
vapor-liquid-liquid-hydrate equilibrium. Compositions of three coexisting fluid
phases have been obtained along eight isotherms at temperatures from (285.15 to
303.5) K and at pressures up to either the upper critical end point (at which
the carbon dioxide liquid-rich and the gas-rich phases become critical) or up
to the hydrate formation locus. Compositions of coexisting vapor and liquid phases
have been also obtained along three isotherms at temperatures from (323.15 to
423.15) K and pressures up to 20 MPa. The quadruple curve
along which hydrates coexists with the three fluid phases was also measured.
experimental data obtained for these ternary mixtures have been compared with
the predictions of the statistical associating fluid theory for potentials of
variable range (SAFT-VR) in which pure-component model
parameters are usually obtained by fitting the theory to the experimental
values of the vapor pressure and saturated liquid densities  and unlike
binary interaction parameters are usually determined by comparison to mixture
this work, we used the SAFT-VR parameters reported previously in the work of Míguez et. al  for the system (methane + carbon
dioxide + water), while the parameters used for the system (n-heptane + carbon
dioxide + water) were obtained in our own analysis. Furthermore, a detailed study
of the ternary mixtures was carried out based on comparison with available data
for the constituent binary subsystems. In this way, we analyzed the observed
effects on the solubility when the third component was added.
E.; Galindo, A.; Trusler, J. P. M., J. Phys. Chem. 2011, 115, 14591.
A.; Galindo, A.; Whitehead, P. J.; Mills, S. J.; Jackson, G.; Burgess, A. N.,
J. Chem. Phys. 1997, 106, 4168?4186.
Míguez, J. M.; dos Ramos, M.
C.; Piñeiro, M. M.; Blas, F. J., J. Phys. Chem.
2011, 115, 9604.
gratefully acknowledge the funding of QCCSRC provided jointly by Qatar
Petroleum, Shell, and the Qatar Science and Technology Park, and their
permission to publish this research.
Keywords: Phase behavior; modeling;
SAFT, hydrocarbon; water, methane, heptane, carbon dioxide.