Page 23 - Hybrid Enhanced Oil Recovery Using Smart Waterflooding
P. 23

CHAPTER 1 History of Low-Salinity and Smart Waterflood  15

          with 5761 ppm. Brines of key ions and smart water have  4.4                         14
                    2þ   2þ       2
          all ions of Ca ,Mg , and SO 4  as well as NaCl. The  4.2                            13
          brine of key ions has 3.5 times higher concentration of                             12
          divalent ions and lower concentration of NaCl than  4.0
          smart water brine. The z-PALS estimates the z-potential  3.8                        11
          of binary systems of brine/oil droplet and brine/calcite.                           10
          Generally, the opposite charge of the binary systems  3.6                           9
          results in the electrostatic attraction between the two in-  3.4                    8
          terfaces of brine/oil droplet and brine/calcite. The
          attraction makes the oil droplet adheres to rock surface.  pCa  3.2                 7  μ Ca 2+  Adsorbed (    moles/gm CaCO 3 )
          When both interfaces have negative charge, an electro-  3.0                         6
          static repulsion occurs and a brine film stabilizes be-                              5
                                                          2.8
          tween the interfaces modifying wettability toward                                   4
          water-wetness. The experiments report that the binary  2.6
                                                                                              3
          system of brine/oil droplet shows the negative z-poten-  2.4
          tial regardless of brine type. In the binary system of                              2
          brine/calcite, the cases of NaCl, Na 2 SO 4 , and smart  2.2                        1
          water show the negative z-potential, but the other  2.0                             0
          show the positive z-potential. The increasing positive  0  2  4  6  8  10 12 14 16 18 20
          z-potential for key ions brine is attributed to the higher  Zeta – potential (mV)
          potential of Ca 2þ  above the potential of SO 4  2  . This  FIG. 1.16 The z-potential of the calcium carbonate
          study also explained that the reason of the positive z-  dispersion system as a function of equilibrium concentration
                                                                               2þ
                                                        of Ca 2þ  and the adsorption of Ca . (Credit: From Huang,
          potential of individual divalent cation brines (CaCl 2
          and MgCl 2 ) is originated from the adsorption of Ca 2þ  Y. C., Fowkes, F. M., Lloyd, T. B., & Sanders, N. D. (1991).
          on the calcite surface or the formulation of a surface  Adsorption of calcium ions from calcium chloride solutions
          layer of Mg-bearing calcite. Referring the Huang,  onto calcium carbonate particles. Langmuir, 7(8):1742e1748.
          FowkesLloyd, and Sanders (1991), adsorption of Ca 2þ  https://doi.org/10.1021/la00056a028.)
          can be explained. Huang et al. (1991) experimentally
          observed  the  proportional  relationship  between  CaCl 2 , MgCl 2 ,Na 2 SO 4 , key ions, and deionized water,
          adsorption of Ca 2þ  and z-potential of calcium carbon-  which were tested in Alotaibi and Yousef (2017). The
          ate dispersion system (Fig. 1.16). It indicates that the  measured z-potentials using the brines from the stream-
          Ca 2þ  could penetrate into hydrolysis layer, substitute  ing potential measurement are compared with that
          the water at calcite surface, and bond at the surface.  from z-PALS technique. The results from z-PALS tech-
          Ayirala, Al-Saleh, Enezi, and Ali (2018) carried out the  nique are referred from Alotaibi and Yousef (2017).
          additional streaming potential measurements to mea-  The streaming potential measurement shows the oppo-
          sure z-potential of binary system with various brines  site z-potentials of the two brines of MgCl 2 and key ions
          and carbonates at different temperatures. It is observed  compared with the z-PALS technique. Although z-PALS
                 2   has a favorable effect on the alteration of  technique results in the positive z-potentials for the
          that SO 4
          z-potential toward more negative and its reactivity  brines, streaming potential measurement shows the
          significantly increases by nearly one order of magnitude  negative potentials. The study explained that the nega-
          in the higher temperature. In addition, the experiments  tive potentials from the streaming potential measure-
          report a few observations regarding roles of cations. The  ment agree well with the results of previous coreflood
          Ca 2þ  has tendency to increase the positive z-potential,  and spontaneous tests (Strand et al., 2006; Zhang &
          but the Na þ  and Mg 2þ  slightly change the potential  Austad, 2006; Zhang et al., 2007). Therefore, the study
          toward less negative. The significant concentration of  concluded that the z-PALS technique is comparable to
          Na 2þ  has the potential to hinder the reactivity of  the contact angle measurement and streaming potential
             2                            2þ       þ    measurement is more appropriate to interpret the
          SO 4  in the high temperature. The Mg  and Na
          have the limited reactivity on carbonate surface regard-  z-potential in coreflood and spontaneous tests.
          less of temperature conditions, and the Ca 2þ  is deter-  Based on the experimental observations, LSWF or
          mined to be the most reactive cation making the  smart waterflood have been deployed in field tests.
          positive z-potential at the carbonate rock surface. The  Next section illustrates the observations of field trial
          study also evaluated the various brines of NaCl,  tests in sandstones and carbonates.
   18   19   20   21   22   23   24   25   26   27   28