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Replicating the pore topology/structure of tight gas reservoirs is essential to model fluid flow through such porous media.
The main input parameters required to model fluid flow through a naturally fractured formation are fracture permeability, fracture porosity and shape factor (Kazemi et al. 1976).
However, most of the researchers have employed numerical simulations to model fluid flow through the fracture/fracture network, or laboratory investigations on intact rock samples with diameter ranging between 38 mm and 45 cm and the diameter-to-length ratio of 1 2 using different experimental methods.
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In a dual-porosity model, fluid flows through the fracture system in the reservoir, while matrix blocks are segregated by the fractures and act as fluid sources for them.
Using a synthetic particle model, viscous fluid flow through packed beds of porous particles is directly simulated at the pore scale (1000Å) using the lattice Boltzmann method to characterize intraparticle and interstitial flow.
In pore-scale modeling of fluid flow through 2D models with the aid of Lattice Boltzmann method, the geometrical domain is divided into regular lattices with similar spacing in both x- and y-directions.
Computational fluid dynamic (CFD) method was used for modeling of fluid flow through the Eulerian multiphase model.
This study will also help in developing dimensionless mathematical models for fluid flow through porous media.
This paper concerns with numerical modeling of fluid flow through a zigzag-shaped channel to be used as the cooling plate for polymer electrolyte membrane fuel cells.
Excess pressure drop induced by inertial effects limits the applicability of Darcy's law for modeling of fluid flow through porous media at high velocities.
Furthermore, this experiment also allows us to extract necessary information for the modelling and simulation of fluid flow through shale rocks at pore scale.
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