Page 66 - Hybrid Enhanced Oil Recovery Using Smart Waterflooding
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58      Hybrid Enhanced Oil Recovery using Smart Waterflooding


                                                                 Disjoining pressure  Oil-wet


                                                        h∞
                    Oil                                                       Initial attractive force
            Ψ1
               h0   Brine                   θ                                    Modified salinity
            Ψ2                                                                   water injection
                                                                 Disjoining pressure  Water-wet  Water film
                   Mineral Surface                                            Final repulsive force







                FIG. 3.13 The schematic description of interaction between oil and rock surfaces and change of attractive
                force to repulsive force owing to variation in electrostatic forces as a result of modified salinity water injection.
                (From Sanaei, A., & Sepehrnoori, K. (2018). Implication of oil/brine/rock surface interactions in modeling
                modified salinity waterflooding in carbonate and sandstone reservoirs. In: Paper presented at the SPE annual
                technical conference and exhibition, Dallas, Texas, USA, 24e26 September. https://10.2118/191639-MS.)
            The validations of the numerical models are per-  measurements. Because the numerical model ignores
          formed by comparing with other experimental works.  the kinetics of calcite dissolution, simulation slightly
          Firstly, the prediction of contact angle is investigated.  underpredicts the effluent concentration of calcium
          The experiments measure contact angle varying pH  against the experiments.
          and composition of brine for both quartz and calcite  Up to date, extensive numerical models have been
          surfaces. The numerical model using the DLVO theory  proposed to describe the LSWF and smart waterflood
          and augmented Young-Laplace equation does not  in sandstone and carbonate reservoirs. There are a few
          exactly match the measured contact angle values, but it  studies to model LSWF following the mechanisms of
          captures the equal tendency in contact angle change  mineral dissolution or fines migration. Hiorth, Cathles,
          against  the  experimental  results.  Secondly,  the  and Madland (2010) numerically assessed the two
          validation of the surface complexation models is  potential  mechanisms  changing  carbonate  rock
          accomplished by investigating and comparing the  wettability: (1) water chemistry changes the charge on
          z-potentials at calcite and oil surfaces, respectively, be-  the rock surface and (2) changes in the water chemistry
          tween the simulations and experimental measurements.  could dissolve rock minerals. The numerical simulation
          Tuning the densities of hydrated calcium and carbonate  investigates how water chemistry influences the surface
          sites of calcite surface, where surface complexation  charge and rock dissolution in pure calcium carbonate
          reactions occur, the numerical model predicts the  rock similar to the Stevns Klint chalk. The first potential
          accurate z-potential on the calcite surface against the ex-  mechanism is validated through the numerical simula-
          periments. In addition, the numerical simulation of oil  tion of LSWF and z-potential calculation. The numerical
          surface complexation model matches the z-potential  model uses the bulk aqueous and surface chemistry
          measured on oil surface by slightly tuning the equilib-  models as well as mineral reactions of precipitation
          rium constant of the surface complexation reactions.  and dissolution. In the numerical model, the concentra-
          Lastly, the numerical simulation of LSWF coreflooding  tion of speciation of surface complexes is predicted. The
          models the experimental work of Chandrasekhar,  adsorption of sulfate ion is also estimated and
          Sharma, and Mohanty (2016). The oil recovery and  compared with the experimental observation of Strand,
          effluent concentrations of ions are compared between  Høgnesen, and Austad (2006). Then, the z-potential
          simulations and experiments. Except for the calcium  using the Grahame equation is calculated and compared
          concentration, productions from the numerical models  with the experimental measurements of z-potential
          are relatively comparable with the experimental  (Strand et al., 2006; Thompson & Pownall, 1989;
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