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Part I: Reservoir Engineering Primer  69



                            8.2 Enhanced Oil Recovery

             Improved recovery technology  includes traditional  secondary recovery
        processes  such  as  waterflooding  and  immiscible  gas  injection,  as  well  as
        enhanced oil recovery  (EOR) processes. EOR processes  are usually classified
        as one of the following processes:  chemical, miscible, thermal, and microbial.
        A brief description  of each of these processes is presented  here. The literature
        on EOR processes is extensive. For more detailed discussions of EOR processes,
        including screening criteria and analyses of displacement mechanisms, see such
        references as Taber and Martin [1983],  Lake [1989], Martin  [1992], Taber, et
        al. [1996], and Green and Willhite [1998].


        Chemical
             Chemical flooding methods include polymer flooding, micellar-polymer
        or  surfactant-polymer  flooding,  and  alkaline  or  caustic  flooding.  Polymer
        flooding is designed  to improve the mobility ratio and fluid flow patterns of a
        displacement process by increasing the viscosity of injected water containing
       polymer,  Micellar-polymer  flooding  uses  a  detergent-like  solution to lower
       residual  oil  saturation  to waterflooding. The polymer  slug  injected after  the
       micellar slug is designed to improve displacement efficiency. Alkaline flooding
       uses alkaline chemicals  that can react with certain types of in situ crude. The
       resulting chemical product is miscible with the oil and can reduce residual oil
       saturation to waterflooding.


       Miscible
             Miscible flooding methods include carbon dioxide injection, natural gas
       injection, and nitrogen  injection. Miscible gas injection must be performed at
       a high enough pressure to ensure miscibility between the injected gas and in situ
       oil. Miscibility is achieved when interfacial tension (IFT) between the aqueous
       and oleic phases is significantly reduced. The desired IFT reduction is typically
       from  around  1 dyne/cm  to  0.001  dyne/cm or  less.  Any reduction  in IFT can
       improve displacement  efficiency, and a near miscible process can yield much
       of the incremental oil that might be obtained from a miscible process. If reservoir
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