Abstract
Abstract
Foamy oil flow appears to be an important contributing mechanism in the better than expected performance of solution gas drives in many Canadian and Venezuelan heavy oil reservoirs. The foamy flow occurs when the gas released from solution during depletion is able to flow through the sand while remaining dispersed in the oil. In laboratory depletion tests, it occurs when a high enough rate of pressure decline is used. With low rates of pressure decline, the depletion appears to occur by the classical two-phase flow mechanism and results in a low recovery factor.
Two types of laboratory depletion experiments were carried out to further examine the conditions needed for initiating foamy flow. First, a series of depletion tests was completed at different rate of pressure depletion to establish the relationship between the rate and the recovery factor. In the second type of experiments, the depletion was started at a low rate and continued to different depletion levels before increasing the depletion rate to a much higher value.
The results show that in tests done at a constant rate of depletion the recovery factor decreases with the decreasing rate of pressure depletion. In the second type of test involving slow depletion followed by fast rate of pressure decline, the recovery factor depends strongly on the pressure level to which the slow depletion was continued. If the slow depletion was continued to level that resulted in the establishment of continuous gas saturation, the subsequent fast rate of depletion was ineffective in providing a high recovery factor. However, when the depletion rate was increased before the average gas saturation in the sand-pack exceeded the critical gas saturation, the recovery factor was much higher and comparable to the tests involving high rate of depletion from the beginning.
These results tend to strongly suggest that the high recovery factor obtained in fast depletion tests is not related to events that take place during the initial phase of depletion, i.e. during the nucleation and initial growth of gas bubbles. It is what happens at the point when the gas phase is ready to become continuous that controls the depletion performance. A plausible explanation is that when the pressure gradient becomes high enough to mobilize the bubbles before they coalesce into a continuous gas phase, the formation of continuous gas phase is delayed. This keeps the gas mobility low and improves the recovery performance.
Introduction
Several laboratory studies have reported a dramatic effect of depletion rate on the performance of solution gas drive in heavy oil systems (Handy, 1958; Sheng et al.,1999; Pooladi-Darvish and Firoozabadi, 1999; Bayon et al. 2002). The recovery factor are reported to be much higher when higher rates of pressure decline are used. Several theories have been postulated to explain this dependence of recovery factor on rate of pressure decline (Firoozabadi, 2001; Shen and Batycky, 1996; Maini 1999; Smith 1988). The most plausible explanation appears to be based on the formation and flow of a gas-in-liquid dispersion that is often referred to as "foamy oil" (Maini, 2001). The dispersed flow of gas delays the formation of a continuous gas phase that would be able to flow at a higher rate and will eventually result in rapid depletion of the reservoir energy. This ability of gas to flow while remaining dispersed in the oil appears to be the mechanism that keeps the gas mobility low during depletion.
Although it is apparent that, in such high rate depletion tests, flow of a gas-in-oil dispersion is involved, the mechanisms involved in the formation of such dispersions are not fully understood. Two schools of thought have emerged to explain the formation of such dispersions. Several authors suggest that such dispersions are formed by nucleation of a very large number of bubbles (Arora and Kovscek, 2001; Claridge and Prats, 1995, Smith 1988). The term "explosive nucleation" has been employed by some to dramatize the situation (Gelikman et al., 1995). What happens beyond the nucleation stage has not been fully delineated. It has been suggested that these bubbles remain smaller than the pore-throat size and are produced with the oil (Smith, 1988).