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Chapter 8: Gas Injection and Fingering in Porous Media
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                           capillary tube (slim tube) at a series of successively higher pressures. If we plot
                           the amount of displaced oil versus pressure, the resulting curve usually has a break
                           at about 95% recovery, the pressure at which is taken as the minimum miscibility
                           pressure. However, we must keep in mind that many crudes contain asphaltenes that
                           precipitate and do not dissolve, even after a series of theoretical multiple contacts
                           between the crude and propagation of the mixture of the injection fluid and the crude’s
                           non-asphaltenic components.
                             In what follows we describe some of the issues that are most important to gas
                           injection processes.


                           8.10.1  Reservoir Characterization and Management
                           In virtually all gas injection projects, the most critical decisions are made only
                           after lengthy computer simulations that attempt to optimize the amounts of the fluid
                           injected, the injection and production rates, and other operation variables. Thus, uti-
                           lizing a realistic model of the reservoir is very important and, in fact, the accuracy
                           of any predictive simulation technique is limited directly by the accuracy with which
                           the reservoir can be described. Despite the extensive sets of experimental data that
                           are used as the input parameters, the sophistication of the simulators, the size of the
                           computers on which the simulations are carried out, and the large number of cases
                           that are simulated, the simulator’s predictions may still be subject to very large uncer-
                           tainties. Therefore, a much less expensive pilot flood is usually carried out first, and
                           the reservoir’s model is tuned by changes in the values of the input parameters in
                           order to make the simulator’s output fit the pilot data.
                             For the field-scale projects that have been carried out, calculated optimal CO 2
                           injection volumes have ranged from 20 to 50% of the hydrocarbon pore volume. The
                           predicted CO 2 utilization factors range from 5 to 15 Mcf CO 2 /bbl of recovered oil.
                           The projected ultimate oil recoveries range from 5 to 30% of the original oil-in-place.
                           These numbers represent only the consensus of the current expectations. Significant
                           revisions of many of these estimates may be required after a large amount of actual
                           full-scale production data become available.


                           8.10.2  Mobility Control
                           As discussed above, the control of unfavorable mobility ratios is recognized as a major
                           technologicalproblemofgas-floodEOR,assuchmobilityratiosproducethefingering
                           phenomena which are a principal reason for the failure of many of the liquefied
                           petroleum gas floods of the 1950s and early 1960s (Craig, 1970). These problems
                           occur because the injection gases have very small viscosities at the temperatures and
                           pressures at which they are used, hence producing an unfavorable mobility ratio. The
                           problems associated with the mobility are greatly aggravated, and their theoretical
                           and experimental study greatly complicated by the facts that, (1) the reservoir rock
                           is highly heterogeneous at every length scale, from sub-millimeter to kilometer, and
                           (2) the number of fluid phases is often three rather than two.
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