CO2 diffusion in the oil phase in the presence of porous
media is of great importance to forecast the performance of enhanced
oil recovery and carbon dioxide capture and storage. When CO2 is brought into contact with an oil phase, diffusion occurs. The
indirect pressure-decay methodology has been applied successfully
to determine the mutual diffusion coefficients of supercritical CO2 and crude oil at temperature of 65 °C. Theoretically,
a one-dimensional double-way mass transfer model incorporating the
capillary and adsorption effects of porous media has been constructed
to quantify the mutual dynamic diffusion coefficients. The crude oil
has been characterized into five pseudo-components for the accurate
description of the phase behavior of CO2 gas and oil phases.
An optimization method along with the PR equation of state is employed
to determine each component’s diffusion coefficients in the
gas and oil phases for the purpose of minimization of the difference
between the experimental data and calculated results. Satisfactory
agreements are obtained with a merely 0.97% pressure difference when
a variable diffusion coefficient is implemented. The short-time experimental
test and a long-time-duration calculation are recommended for further
diffusion investigation. The capillary analysis gave a regressed fractal
dimension of 2.7049 with the average absolute deviation of 0.602%.
The adsorption phenomenon can be greatly influenced by the existence
of heavy components. The heavier the components, the greater their
impact on adsorption. Furthermore, a faster and enhanced diffusion
process is observed at high pressure and temperature. The combination
of several complex mechanisms leads to the initial gradual increase
of the diffusion coefficient with time, and then, it arrives at a
plateau, which is slightly different from the previous diffusion coefficient
changing tendency mentioned in the literature. In the presence of
a low-permeability formation core, the determined diffusion coefficients
of CO2 in the gas and liquid phases are increased from
4.38 × 10–9 to 6.21 × 10–9 and 6.16 × 10–10 to 9.21 × 10–10 m2/s when the system pressure is decreased from 18.2
to 12.11 MPa, respectively. In addition, the capillary effect can
lead to a reduction of the diffusion coefficient in the oil phase
but has little effect on the diffusion coefficient in the gas phase.