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72                             Enhanced Oil Recovery in Shale and Tight Reservoirs


          respective Winprop and GEM simulators developed by Computer
          Modeling Group.
             The Winprop simulator uses the asphaltene precipitation model pro-
          posed by Nghiem et al. (1993). The model splits the heaviest component
          into two components: the nonprecipitating component and precipitating
          component. The two components have the same critical properties and
          acentric factors but different interaction coefficients with light components.
          The precipitating component has relatively larger interaction coefficients
          with light components, which leads to greater incompatibility between
          the precipitating component and the light components. As a result, the
          precipitating component will transfer to a solid phase, and thus precipitate.
          The nonprecipitating component includes heavy paraffin, resins, asphal-
          tene/resin micelles that will not dissociate. The precipitating component
          is asphaltenes and asphaltene/resin micelles that could dissociate and precip-
          itate. The precipitating asphaltene component in crude oil is considered as a
          pure dense phase which can either be a liquid or solid. This phase is referred
          to as the asphalt phase.
             Shen and Sheng (2018) lumped together 24 components of an oil into
          five pseudocomponents: C 3 4 ,C 5 8 ,C 9 19 ,C 20 40 ,C 41þ . The heavy
          precipitating component was C 41 asphaltene . The interaction coefficients of
          the split precipitating asphaltene component with the light components
          and the molar volume of asphaltene phase were tuned to match the asphal-
          tene precipitation data from the model with the experimental data. The
          tuned parameters are listed in Table 3.1. The predicted asphaltene precipi-
          tation data and the experimental data are compared in Fig. 3.13. The molar
          volume of precipitating asphaltene component was tuned to be 0.92 L/mol.
             The GEM simulator uses the asphaltene deposition model developed by
          Wang et al. (1999):

                        vE A
                            ¼ aC A f   bE A ðv L   v Lc Þ þ gu L C A   (3.1)
                         vt
             The first term on the right side of the above equation is the surface depo-
          sition. a is the surface deposition rate coefficient that should be a positive



          Table 3.1 Binary interaction coefficients between asphaltene component and other
          components used in the precipitation model.
          Components  CO 2  CH 4  C 3L4  C 5L8  C 9L19  C 20L40  C 41D  C 41 asphaltene
                      0.27  0.2  0.2   0.04  0     0       0     0
          C 41 asphaltene
   80   81   82   83   84   85   86   87   88   89   90