Page 112 - Hybrid Enhanced Oil Recovery Using Smart Waterflooding
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104     Hybrid Enhanced Oil Recovery using Smart Waterflooding

          tertiary recoveries of coreflooding. The crude oil has  injection of Flopaam 3630s polymer slug follows the
          TAN of 0.15 mg KOH/g and TBN of 1.29 mg KOH/g.  surfactant slug injection. The coreflooding experiments
          The formation water of 231,194.9 ppm TDS and syn-  are designed with secondary waterflood, and tertiary
          thetic water of 14,063.3 ppm TDS are prepared. The  surfactant flood followed by polymer flood. The core-
          synthetic water is modified to make the low-salinity  flooding experiments use high- and low-salinity
          and low-hardness alkaline solution by extracting the  makeup brines. As observed in the previous studies
          divalent cations and adding the chemical additive.  of LSPF, the polymer has less degradation in low
          Two samples of low-salinity and low-hardness alkali so-  salinity condition to reach the target viscosity. Less
          lutions with different concentrations of chemical addi-  polymer concentration by a factor of 2 is required for
          tive are prepared. The diluted synthetic water of  the low-salinity polymeric solution compared with
          3587.45 ppm TDS is also investigated. As the salinity  the high-salinity polymeric solution. The polymer
          decreases and pH increases, both IFT and contact angle  slug injection increases the differential pressure regard-
          decrease. The results of IFT and contact angle measure-  less of salinity condition. Despite the less polymer con-
          ments indicate that the acidic component of crude oil  centration,  significantly  higher  increment  of
          reduces the IFT at high pH condition and modifies the  differential pressure is observed in LSPF compared
          wettability. In the adsorption test, the low-salinity and  with the polymer flood using high salinity. It implies
          low-hardness alkali solution shows slightly higher  the higher injectivity to be secured for LSPF. Before
          adsorption  than  the  synthetic  seawater  and  the polymer slug injection, the surfactant slug size of
          low-salinity water, but the discrepancy is acceptable.  0.5 PV is designed to be injected. During the surfactant
          The stability test of emulsion measures the separation  injection with small slug size, oil recovery negligibly or
          efficiency of water from emulsion system for the  hardly increases. However, the succeeding polymer
          low-salinity water and low-salinity and low-hardness  flood produces immobile oil because of the prein-
          solutions. Lower separation efficiency is observed for  jected surfactant additive (Fig. 4.35) and reduces
          the alkali solutions compared with the low-salinity wa-  717% of residual oil saturation. It is obviously
          ter. It implies that the low-salinity and low-hardness  concluded that low salinityeaugmented surfactant/
          alkali solution generates more stable water-in-oil  polymer flood has enough potential to produce the
          emulsion. In addition, it results in less swelling of  trapped oil by improving both displacement and
          bentonite. With the favorable aspects of low-salinity  sweep efficiencies. Synergetic effects between LSPF
          and low-hardness alkali solution, higher oil recovery  and LSSF can be secured through low salinitye
          is obtained in displacement experiments compared  augmented surfactant/polymer flood (LSSP) as well
          with the waterflood and LSWF.                  as low chemical injection.
                                                          Wang, Ayirala, AlSofi, Al-Yousef, and Aramco (2018)
                                                        published the experimental attempts of LSSF for the car-
          ALKALINE-SURFACTANT-POLYMER FLOOD             bonate oil recovery. The connate water has salinity of
          The chemical EOR has a huge potential to employ the  213.723 mg/L TDS, and the high-salinity water has
          synergetic effects by incorporating the low-salinity wa-  salinity of 57,610 mg/L TDS. The low-salinity water is
          ter or smart water as the makeup brine. Although the  prepared by diluting the high-salinity water by a factor
          mechanism and effect of LSWF are not fully clarified,  of 10. A sulfonated polyacrylamide and betaine-type
          the LSWF obviously plays positive roles on the stability  amphoteric surfactant are used. The contact angle and
          of chemical, adsorption of chemical, formation dam-  z-potential are measured to confirm the potential of
          age, optimum condition for the chemical EOR, etc.  wettability modification in low-salinity water condition
          With the clear evidence of the synergy between LSWF  for the specific carbonate rock. The reduction in contact
          and single chemical EOR process, the coapplications  angle and decrease toward more negative z-potential are
          of alkaline, surfactant, and polymer flood to be com-  observed in low-salinity water condition compared
          bined with the LSWF are further investigated to enhance  with the high-salinity water condition. These observa-
          the synergy.                                  tions consistently agree with the previous experimental
            Previously, Johannessen and Spildo (2014) re-  results of LSWF. It is evaluated that the LSWF modifies
          ported an enhanced potential to reduce IFT by the  the wettability of carbonate rock from oil-wet to weakly
          LSSF and the higher oil recovery from sandstone core-  oil-wet or intermediate wet. With the evidence of LSWF
          flooding with the comparable capillary number  effectiveness, the tertiary LSSP application is evaluated
          improvement. In the coreflooding experiment, poly-  and compared with the conventional surfactant-
          mer slug injection is applied to support the LSSF. The  polymer flood using high-salinity water as makeup
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