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Reading Room :: Theses 1995

Charles Partogi Siallagan's thesis Precalculation of A Streamline Model Simulator For Micellar Displacement

by
Charles Partogi Siallagan,, M.S.E.

University of Texas at Austin, 1995
Supervisor: Ben H. Caudle

The objective of this study is to develop a streamline model simulator for micellar slug displacement, a concentrated, surfactant-stabilized dispersions of water and hydrocarbon that are used to enhance oil recovery. In this displacement, several banks of miscible fluids are developed. The micellar slug displacement process is characterized by a zone of intermediate fluid which is miscible with the reservoir oil at its leading edge, and is miscible with the injected fluid, as a driving fluid, at its trailing edge.

At each time step on each center pathline, the positions of each front are included in the calculation of each front pressure in order to determine conductivity ratio for the unequal mobility treatments. The conductivity ratio effect on the frontal velocities is measured at constant pressure in order to control the displacement. Since all of the fluid interface points must be moved over the same time step, this time step should be calculated using the highest total velocity value of moving fronts. The change in the flow rates into each streamline is accounted for as a function of mobility ratio. The simulator can model a stratified reservoir and use the Dykstra-Parson's method for permeability distribution. It is also capable of modeling areal sweep for a field having multiple wells, arbitrary well patterns, an irregular boundary, and an isotropic or anisotropic reservoir.

The method utilized for bounding the irregular boundary is the use of arbitrarily placed guard or bounding sources.

The streamline model, in conjunction with fractional flow theory and piston like displacement assumptions, provides an alternative way to predict the performance of micellar slug displacement with limited input data and computation time.

The miscible displacement will change into immiscible displacement for the time of the process. Loss of miscibility is determined by using the position between the slug front and water front. The sensitivity of the oil recovery was investigated using micellar displacement and process variables.

Finally, the simulator has been applied to a small depleted field scale condition. The Kellyville Field, located in Creek County, Oklahoma was used to demonstrate that the model is capable of handling a field problem.

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