Page 79 - Fundamentals of Enhanced Oil and Gas Recovery
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67
             Enhanced Oil Recovery Using CO 2

                                                     C 1  S = Injected solvent composition
                                                          O = Reservoir oil composition
                                                         S


                                                         V 1
                                                          V   V
                                                           2   3
                                                               V
                                      Tie lines                 4
                                                 M
                                                  1
                                                      M
                                                       4
                                                    M
                                         L        M  3    Critical point
                                          1        2
                                           L 2
                                         O
                                             L  L
                                              3  4
                                                       Critical tie line
                                C 7+                                      C –C 6
                                                                           2
                   Figure 3.4 Representation of undeveloped miscibility during VGD process [29].
                   generated for the selected solvent. As shown in Fig. 3.4, the process of enrichment
                   continues till the mixing line will be along a tie line. Enrichment then ceases, result-
                   ing in an immiscible process.
                      The limiting criteria for a multiple-contact process to be miscible through vapori-
                   zation are determined by the so-called critical tie line. This line is tangent to the
                   binodal curve at critical point. Conceptually, for a gas flooding process to be miscible
                   through multiple contacts with VGD, the oil composition should lie on or to the right
                   of critical line and injected fluid composition should lie to the left. This means that
                   oil should be rich in intermediate components, while injection fluid can be a dry gas.
                      Consider Fig. 3.5—it represents the condensation gas drive process on a ternary
                   diagram. Through this process, the solvent contacts the oil and some of gas compo-
                   nents will condense and transfer to the oil phase. As a result, oil phase composition
                   changes till it gets completely miscible with the gas phase. Similar to vaporization gas
                   drive, miscibility will not occur for all combinations of solvent and reservoir oil. The
                   limiting criteria is the critical tie line. Based on this criteria, the oil composition
                   should lie to the left side of the critical tie line and injected fluid composition should
                   lie to the right. In other words, oil should contain heavy components, whereas the
                   injected fluid should contain a significant amount of intermediate components rather
                   than being a dry gas. Fig. 3.6 shows a typical condition in which miscibility will not
                   be generated.

                   3.2.1.2.1 Liquid (Vapor) Dropout
                   During vaporization process, there can be a liquid dropout behind the front. Once
                   again, consider Fig. 3.3—the interface of new gas phase (V 1 ) and injection gas (S) is
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