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Fluid-rock interactions                                      201


              solution (NaOH) are also presented in this figure. It shows that no oil was
              recovered from the brine, indicating the core was non-water-wet; the oil
              recovery was the highest for the high-pH solution, probably the NaOH
              solution reacted with the crude to have generated some surfactant. The initial
              low rate of oil recovery from the high-pH brine was due to the lower inter-
              facial tension which resulted in lower capillary pressure as a main drive force.
                 Takahashi and Kovscek (2009) also conducted forced displacement
              experiments. The final oil recovery factors were 65%, 70%e80%, and
              95% for the neutral pH brine, low-pH and carbonated water, and high-
              pH brine, respectively, as shown in Fig. 8.24. The highest oil recovery for
              the high-pH brine was attributed to the lower interfacial tension.
                 Moore et al. (2017) studied the fracture permeability of a fractured
              Bakken shale sample and a fractured Marcellus shale sample exposed to
              liquid CO 2 flow. The confining pressure was 3000 psi (20.68 MPa) and
              the pore pressure was 1000 psi (13.79 MPa). They observed that the fracture
              permeability was reduced several times to tens of times as the cores were
              exposed to the liquid CO 2 for up to over 300 h. However, they concluded:
              “CO 2 does not appear to reduce intrinsic fracture permeability signifi-
              cantly.” Those shale samples did not have a high account of swelling min-
              erals. It was implied that swelling minerals would reduce matrix and fracture
              permeabilities.
                       1
                      0.9

                      0.8
                      0.7
                     OlP recovered  0.6
                      0.5

                      0.4
                      0.3
                                                          Brine
                                                          Carbonated water, No.1
                      0.2                                 Carbonated water, No.2
                                                          HCI brine (pH3), No.1
                      0.1                                 HCI brine (pH3), No.2
                                                          NaOH brine (pH12)
                       0
                        0    1   2    3    4    5   6    7    8   9    10
                                               PVI
              Figure 8.24 Oil recovery of forced displacement using different pH brines (Takahashi
              and Kovscek, 2009).
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