Page 81 - Hybrid Enhanced Oil Recovery Using Smart Waterflooding
P. 81

CHAPTER 4   Hybrid Chemical EOR Using Low-Salinity and Smart Waterflood  73


            Vermolen, Pingo Almada, Wassing, Ligthelm, and  the extra cost in OPEX/CAPEX for the desalination is
          Masalmeh (2014) validated the prospective benefits  much lower than the saving in OPEX for the less poly-
          and synergetic effects, which can be drawn for LSPF. It  mer injection, securing chemical stability of polymer us-
          is summarized that the low salinity makeup brine can  ing low-salinity makeup water significantly increases
          secure a number of benefits to polymer flood: (1) chem-  the economics of LSPF. The second experiment evalu-
          ical stability; (2) mechanical stability, especially, at high  ates the viscosity loss by the mechanical degradation
          temperature condition; (3) less adsorption; and (4) less  at different shear rate and salinity conditions. The exper-
          scaling and souring problems. The benefits provide less  iment calculates the degree of polymer degradation,
          amount of polymer required to reach the target viscosity  and it is observed that the viscosity loss by shear force
          as observed in previous studies. In addition, it is sug-  increases with an increase in salinity as shown in
          gested that the LSPF introduces the mechanism of  Fig. 4.6. The third experiment using dynamic (oscilla-
          LSWF and using low-salinity water of makeup brine en-  tory) frequency sweep measurements analyzes the
          hances the elasticity of polymer. The mechanism of  viscoelasticity of polymer varying polymer concentra-
          LSWF confidentially modifies the wettability of reser-  tion at different salinity conditions. It measures the rela-
          voir. In addition, the elastic behavior of polymer poten-  tion between storage (elastic) modulus and loss
          tially reduces the residual oil saturation. Because of the  (viscous) modulus and determines the relaxation time
          wettability modification and more reduction in residual  of the polymer from the relation. The higher relaxation
          oil reduction, the LSPF can enhance the displacement  time is observed with decreasing salinity, which means
          efficiency compared with the conventional polymer  the increasing viscoelastic characteristics of polymer.
          flood. This study tried to demonstrate the benefits by  The increasing viscoelastic characteristics of polymer
          measuring the polymer behavior under various condi-  mobilize the immobile oil and potentially increase
          tions. The first experiment of the study measures the  the oil recovery. The polymer adsorption during LSPF
          amounts of HPAM polymer concentration to reach  is also briefly investigated in two aspects. Firstly, the
          the target viscosity of polymeric solution at the different  low-salinity water as makeup brine leads to the less
          salinity conditions of 7000 and 700 ppm TDS. About  adsorption of polymer and the degree of the reduction
          half amount of polymer is required to reach the target  varies with polymer and rock types. Secondly, the effect
          viscosity with 50 cp at a shear rate of 11.5 s  1  in low  of mixing between displacing and displaced brines on
          salinity compared with the high salinity conditions.  the adsorption is investigated. When the low-salinity
          Another experiment estimates 34 times reduction in  polymeric solution displaces high-salinity connate
          polymer concentration at the salinity of 1500 ppm  water, polymer adsorption occurs and polymer propa-
          TDS compared with the 260,000 ppm TDS. Because  gation is retarded. Until the polymer adsorption reaches


                             70%
                             60%

                             50%
                            Degradation  40%                              100 ml/min

                             30%
                                                                          150 ml/min
                             20%                                          200 ml/min
                             10%
                              0%
                                 0  1000 2000 3000 4000 5000 6000 7000
                                           Salinity (ppm TDS)
                FIG. 4.6 Shear degradation of viscosity of polymeric solution at different share rates and salinity conditions.
                (Credit: From Vermolen, E. C. M., Pingo Almada, M., Wassing, B. M., Ligthelm, D. J., & Masalmeh, S. K. (2014).
                Low-salinity polymer flooding: Improving polymer flooding technical Feasibility and economics by using low-
                salinity make-up brine. Paper presented at the International petroleum technology conference, Doha, Qatar,
                19e22 January. https://doi.org/10.2523/IPTC-17342-MS.)
   76   77   78   79   80   81   82   83   84   85   86