Page 113 - Hybrid Enhanced Oil Recovery Using Smart Waterflooding
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CHAPTER 4   Hybrid Chemical EOR Using Low-Salinity and Smart Waterflood  105


                       100                                                       900
                                   LS                         LSP
                        90                                                       800
                                                0.5PV
                        80                      LSS slug
                                                                                 700
                      Oil recovery [% OOIP]  60                         WBT      500  dP [mbar]
                        70
                                                                                 600
                        50
                                                                                 400
                        40
                        30
                                                                                 200
                        20                                              Oil recovery  300
                                                                        dP       100
                        10
                         0                                                       0
                          0       1       2      3       4      5       6       7
                                              Injected volume [PV]
                FIG. 4.35 The oil recovery and differential pressure of coreflooding of low salinityeaugmented surfactant/
                polymer floods. (Credit: From Johannessen, A. M., & Spildo, K. (2014). Can lowering the injection brine
                salinity further increase oil recovery by surfactant injection under otherwise similar conditions? Energy and
                Fuels, 28(11), 6723e6734. https://doi.org/10.1021/ef500995y.)

          brine. The LSSP is designed with the coinjection of poly-  on the synergetic effects and mechanisms of the hybrid
          mer and surfactant additives. The polymer concentra-  ASP process. The studies (Dang, Nghiem, Nguyen, et al.
          tion to be injected in LSSP halves but has the 70% of  2018; Farajzadeh, Matsuura, Batenburg, & Harm, 2012;
          target viscosity compared with the chemical solution  Ghadami, Deo Tewari, Zarubinska, & Motaei, 2018;
          of conventional surfactant-polymer flood. In terms of  Hosseini-Nasab, Padalkar, Battistutta, & Zitha, 2016;
          surfactant, the equal concentration of surfactant is  Nghiem, Skoreyko, Gorucu, Dang, & Shrivastava,
          used for both low- and high-salinity water conditions,  2017) have developed the mechanistic simulation of
          and comparable IFT reduction is observed. The hybrid  ASP process to be coupled with fully geochemical reac-
          LSSP shows the higher oil cut and differential pressure  tions. Based on the comprehensive studies of ASP pro-
          despite less polymer injection. This study also demon-  cess, the application of low-salinity water/smart water
          strated that the hybrid LSSP improves both sweep and  as the makeup brine is implemented into the hybrid
          displacement efficiencies and secures the practicality  ASP process. Reducing the salinity, ionic strength might
          and economics of chemical EOR process.        be optimistic for polymer flood but might not be for
            The hybrid alkaline/surfactant/polymer flood (ASP)  surfactant and alkaline floods owing to optimum
          has been widely investigated because of a number of  salinity condition. Reduction in hardness could bring
          reasons. This hybrid process improves both sweep and  the overall positive benefits to chemical EOR.
          displacement efficiencies and highly enhances the oil  Therefore, many studies have investigated hybrid ASP
          production. The alkali addition produces the in situ sur-  process optimizing the salinity, hardness, ionic compo-
          factant generation, which means the less injection of  sition, etc.
          expensive surfactant. It also reduces the adsorption of  Battistutta, van Kuijk, Groen, and Zitha (2015) con-
          surfactant on the rock surface at high pH condition  ducted the comprehensive experiments of ASP process.
          and secures the stability of surfactant by reacting with  The study estimated the optimal salinity to make the
          the divalent cations. The application of low-salinity  Winsor type Ⅲ of microemulsion as the 1.5 wt%
          water as makeup brine into the hybrid ASP process is ex-  NaCl. At the optimal salinity, the ultralow IFT is ob-
          pected to employ the additional synergy of low-salinity  tained from the IFT measurement and phase behavior
          water and chemical additives, as discussed in previous  test. A variety of ASP formulations are designed. The
          sections, and enhance wettability modification into  makeup brines of the ASP formulations have the salin-
          ASP process.                                  ities of 0.5, 1, 1.5, and 2.0 wt% NaCl. Because the
            Because the mechanisms of ASP processes are sensi-  optimal salinity is determined as 2.0 wt%, the ASP for-
          tive to the salinity, pH, etc., a number of studies have a  mulations having the salinity less than 2.0 wt% are at
          primary object to quantify the effects of geochemistry  underoptimum salinity condition representing Winsor
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