REAL PORE FLOWS · Towards the deterministic modelling of immiscible flows in porous media: Mesoscale simulations and Experimental verification
FP7 — People (Marie Curie Actions)
- Duration
- 2010-09-01 → 2012-08-31
- EU contribution
- €230,747
- Participants
- 1
- Scheme
- MC-IEF
Lines connect the coordinator with its partners.
Results in brief
Towards the deterministic modelling of immiscible flows in porous media: mesoscale simulations and experimental verification
The REAL PORE FLOWS project focused on the study of pore scale transport phenomena during the isothermal evaporation of volatile hydrocarbons from porous media, as well as the dynamics of non-aqueous phase liquids (NAPLs) during immiscible flows. This was achieved through an integrated approach combining targeted experiments and state-of-the-art modelling tools. In the case of drying, we performed a series of experiments with glass bead packings saturated by liquid pentane / hexane or heptane in predominantly two-dimensional (2D) glass cells under environmental conditions to study the dynamics of the drying process and identify the major transport mechanisms. Our experimental setup allowed for the monitoring of the bulk liquid and gas phase distribution patterns, as well as the liquid films that form at the pore walls after the invasion of the bulk gas phase. We were thus able to classify the drying pore space into three distinct regions: - a far-field completely-wet region, where the pore space is saturated by the bulk liquid hexane; - a completely dry region, close to side of the medium open to the ambient environment, that contains only hexane vapours; and - an intermediate region, located between the first two, that is partially saturated by liquid hexane in the form of liquid films at the walls of the pores and by hexane vapours in the central part of the pore space. Based on our experimental results, we proposed a pore network model that accounts for all major transport mechanisms within the porous medium coupled with mass transfer by diffusion through a mass boundary layer over the external surface of the medium. We showed that in the limit of a gravity-stabilised percolation front (interface between the completely wet and film regions) the medium can be treated as a 1D continuum where analytical solutions to the governing equations are derived. We are thus able to obtain results for the drying rates, the critical saturation and the extent of the film region with respect to the various dimensionless numbers that describe the process; the Bond number, a film-based capillary number and the dimensionless extent of the mass boundary layer. In the case of NAPLs undergoing immiscible displacement through a permeable porous medium at high capillary numbers, we proposed a convenient lattice Boltzmann algorithm for the solution of the flow problem in stochastically reconstructed porous domains. In a typical configuration, the non-wetting phase flows through the porous medium in the form of blobs under the combined action of capillary, viscous and gravity forces. We found that the process is governed by the dynamical coalescence and breaking up of blobs, that result in two interacting populations of mobile and stranded blobs, that continuously exchange mass between them. At steady state, when the rates of blob breaking up and coalescing become equal, both populations follow a log-normal size distribution with an average size and cumulative volume that depends strongly on the applied Bond number. At higher Bo numbers, the ratio of mobile to stranded blob saturation increases significantly, as gravity forces overcome capillarity as fluid-fluid interfaces move through pore bodies, and the breaking rate increases, leading to a smaller average blob sizes. Our simulations showed that the transition between single and 2-phase flow occurs when a critical value of the Bond number is applied, and then the mobile blob volume increases non-linearly with Bo until viscous forces become dominant in the system. Three flow regimes are identified; a single phase Darcy-type regime at low Bond numbers, an non-Darcy 2-phase flow regime at intermediate values of Bo, where the Capillary number scales as Ca Bo2, and a Darcy type 2-phase regime at higher values of Bo. These results are in reasonable agreement with recent experimental and theoretical works.
Data: CORDIS, © European Union
Project objective
Immiscible two-phase flow in macroporous materials is a subject of significant applied and scientific interest. It is encountered in a series of environmental and energy-related processes such as soil remediation, enhanced oil recovery from fractured petroleum reservoirs, geothermal processes, CO2 sequestration etc. The study and optimization of such processes requires the development of rigorous modelling tools that successfully capture the physics of the flow process at the pore scale, and the careful setup of experimental studies to verify the precision of these tools. The proposed research aims at advancing the state-of-the-art in this direction through an integrated approach combining numerical and experimental techniques. The modelling of such processes will be based on a mesoscale description of the flow field within porous materials using a thermodynamically consistent Lattice-Boltzmann model that accounts for the interfacial physics and wetting properties from first principles. The complicated structure of the porous materials will be represented by digital domains constructed using a stochastic reconstruction method that reproduces the statistical properties of real porous media. This numerical approach will be validated through a series of experiments in mechanically engineered 2D porous domains, produced according to predefined specifications using a computer controlled etching machine. An experimental apparatus for controlling and monitoring the immiscible flow process through the domains will be used for the study of the population dynamics of Non Aqueous Phase Liquid blobs (NAPL’s) in oil/water systems and the construction of relative permeability curves. The proposed approach is expected to offer significantly improved quantitative results compared to other methods commonly used in these processes that lack this amount of detail in the description of both the flow problem and the representation of the medium.
Original text from CORDIS.
Participants
- CENTRE NATIONAL DE LA RECHERCHE SCIENTIFIQUE CNRS · ParisCoordinatorFrance
Links
Data: CORDIS, © European Union
