Abstract

The effect of injection brine salinity on the displacement efficiency of low water salinity flooding was investigated using sea water at 35,000 ppm, and two field injection waters, namely, Um-Eradhuma (UER) at 171,585 ppm and simsima (SIM) at 243,155 ppm. The salinity of the employed waters was varied from original salinity to 1,000 ppm and used in the displacement of oil in selected core samples. The results of this set of experiments revealed that UER salinity of 5,000 ppm is the optimum system for the candidate reservoir. UER original water and its optimum water were then used in this project as the high and low salinity waters in the CO2–WAG flooding experiments. Displacement efficiencies were evaluated under three injection modes: carbon dioxide WAG miscible flooding (CO2–WAG, 1:1, 2:1, and 1:2), continuous CO2 injection, and waterflood. The WAG performance parameters, such as secondary and tertiary displacement efficiencies, CO2 flood utilization factor, and CO2 performance during different WAG flood cycles were determined. To insure miscibility condition between the injected gas and the employed oil, all of the flooding experiments were conducted at 3,200 psia (which is 300 psia above the minimum miscibility pressure of CO2 and used oil) and 250 °F. Experimental results indicated that core length is a critical parameter in determining the optimum WAG process, and that a minimum core length of 29 cm is required to insure the generation of miscibility before breakthrough in CO2–WAG flooding experiments. On the other hand, core length had no effect on the performance of the low salinity flooding experiments. Using single core flooding low salinity CO2–WAG of 1:2 flooding produced an improvement in the displacement efficiency of 29 % over the high salinity system. Also, composite core flooding experiments showed that the high salinity CO2-2:1 WAG achieved a displacement efficiency of 98 %. These results indicate that achieving miscibility at the reservoir conditions is the dominant mechanism and that low salinity will have no major effect on the displacement efficiency of CO2-Miscible WAG flooding. Results also indicate that oil recovery during different CO2–WAG cycles is a function of WAG ratios.

Highlights

  • The main goal of any enhanced oil recovery (EOR) method is to increase the capillary number providing ‘‘favorable’’ mobility ratios (M \ 1.0)

  • Experimental results indicated that core length is a critical parameter in determining the optimum WAG process, and that a minimum core length of 29 cm is required to insure the generation of miscibility before breakthrough in CO2

  • Composite core flooding experiments showed that the high salinity CO2-2:1 WAG achieved a displacement efficiency of 98 %. These results indicate that achieving miscibility at the reservoir conditions is the dominant mechanism and that low salinity will have no major effect on the displacement efficiency of CO2-Miscible WAG flooding

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Summary

Introduction

The main goal of any enhanced oil recovery (EOR) method is to increase the capillary number providing ‘‘favorable’’ mobility ratios (M \ 1.0). The capillary number (Abrams 1975) is defined as the ratio of viscous to capillary forces. Viscous forces Capillary forces ml r cos h ð1Þ where m and l are the velocity and viscosity, respectively of the displacing fluid, r is the oil–water interfacial tension and h is the contact angle between the oil–water interface and the rock surface measured between the rock surface and the denser phase (water in this case). The overall efficiency of any EOR process depends on both the microscopic and macroscopic sweep efficiencies. While the fluids density difference and rock heterogeneity affect the macroscopic efficiency, the microscopic displacement efficiency is influenced by the interfacial interactions involving interfacial tension and dynamic contact angles

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