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CHAPTER 4   Hybrid Chemical EOR Using Low-Salinity and Smart Waterflood  69


                      1000
                                 Unified viscosity model
                                 Bulk shear viscosity [Delshad et al.(2008)]
                                 Apparent viscosity [Delshad et al.(2008)]
                       100       Carreau model
                      Viscosity [cP]





                        10






                         1
                         0.01      0.1        1        10        100      1000      10000
                                                           –1
                                                   Shear rate [s ]
                FIG. 4.2 The description of viscoelastic behavior of Flopaam 3630s as a function of shear rate. (Credit: From
                Kim, D. H., Lee, S., Ahn, C. H., Huh, C., & Pope, G. A. (2010). Development of a viscoelastic property database
                for EOR polymers. Paper presented at the SPE improved oil recovery Symposium, Tulsa, Oklahoma, USA,
                24e28 April. https://doi.org/10.2118/129971-MS.)

          adsorptions of nonionic and anionic polymers decrease  permeability reduction to shut off water channeling
          with an increase in the temperature. The mechanism of  through high-permeable zones and water conning
          temperature-dependent adsorption of nonionic poly-  from the adjacent aquifers. The permeability reduction
          mer is different to that of anionic polymer. For the  by the polymer adsorption mainly occurs in water rela-
          nonionic polymer, the adsorption is mainly attributed  tive permeability rather than oil relative permeability. It
          to the attraction by the hydrogen bond. Because the  is known as the mechanism of the disproportionate
          increasing temperature breaks up the hydrogen bond,  permeability reduction (DPR). There are a number of
          the attraction between nonionic polymer and rock sur-  gels: movable gels, pH-sensitive polymer, BrightWater,
          face becomes weak, resulting in less adsorption. For the  Microball, preformed particle gel (PPG), etc.
          anionic polymer, higher temperature increases the
          negative charge on the rock surface. The increased elec-  Low SalinityeAugmented Polymer Flood/Gel
          trostatic repulsion between the polymer and rock sur-  Treatment
          face results in the less adsorption of anionic polymer.  Experiments: polymer flood
                                                        Ayiralaetal. (2010) developed the desalination scheme
          Permeability reduction                        for Designer Water developed by Shell. The desalination
          The adsorption of polymer potentially reduces perme-  scheme is designed to formulate the desired injection wa-
          ability or blocks pore throat. There are a number of  ter composition to suit the formation condition. Using
          terms to describe the permeability reduction (Sheng,  the desalination scheme, the conventional polymer
          2011): (1) permeability reduction factor (R k ), which is  flood can be advanced through incorporating the low-
          the ratio of permeability when water flows to the  salinity water as makeup brine. The advanced polymer
          permeability when aqueous polymer solution flows;  flood using the low-salinity water is the hybrid low
          (2) residual resistance factor (R RF ), which is the ratio  salinityeaugmented polymer flood (LSPF). In the LSPF
          of water mobility before to after polymer flood; and  process, the cost-competitive LSWF compared with the
          (3) resistance factor (R F ), which is the ratio of polymer  other EOR methods can bring a couple of benefits to
          mobility to the water mobility during polymer flow.  the expensive polymer flood. The study investigated the
          The cross-linked polymers and gels exploit the  benefits when the polymer flood exploits the low-
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