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70                                                                      Ramin Moghadasi et al.


                   injection gas. This prevents the development of miscibility between injected gas
                   and reservoir oil, as it was about to happen through CGD. However, if these all
                   occurred, the process would not be very efficient. Fortunately, there is a positive
                   mechanism as explained in subsequent lines.
                •  After some periods of injection, some of the oil will be rich in light intermediates.
                   Thus as it contacts fresh gas, less condensation occurs. Nonetheless, the gas phase will
                   strip some middle intermediates from the oil. As a result, the gas phase gets rich in
                   both light and middle intermediates. This gas will contact the oil while stripping less
                   middle intermediates, still losing light intermediates. Such a combination of vaporiza-
                   tion/condensation continues until miscibility is developed in an efficient way.


                3.2.1.2.3 Minimum Miscibility Enrichment
                As discussed before, pressure would modify phase behavior and miscibility can be
                obtained for a combination of solutions that were not miscible previously. However,
                there is an alternative to changing pressure for miscibility to be reached. This alternative
                deals with injection fluid composition alternation. For instance, in a condensing gas
                process, injection fluid composition could be enriched to a minimum amount at which
                the critical tie line passes through its composition. This is to be done at a fixed pressure.
                This minimum enrichment is called the minimum miscibility enrichment (MME). As
                shown in Fig. 3.7, the miscibility at fixed pressure can only be obtained through enrich-
                ment process to MME. In this typical example, the injection fluid will be enriched with
                light intermediates, which decreases the density difference between reservoir oil and
                injection fluid. Indeed, this means more similarity between the oil and injection fluid.

                                                 C 1  S = Original injected solvent composition
                                                     O = Reservoir oil composition
                                                     S
                               Two-phase envelope
                                    P = P 1                MME







                                                     Critical point

                                    O
                                                Critical tie line


                             C +                                    C –C 6
                                                                     2
                              7
                Figure 3.7 MME on ternary diagram [29].
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