REACTIVE TRANSPORT MODELING OF EFFECTS OF CO2 INJECTION WITH VARIABLE IMPURITIES ON DEEP SALINE RESERVOIRS
Effects of injection of impurities on the reservoir mineralogy and brine chemistry are more pronounced upon injection of the oxidizing mix. Simulations without rock-water interactions predict that low pH of around 1 will occur in the vicinity of the injection well and SO42- and NO3- will accumulate at the boundary between very high gas saturation and mixed saturation. When minerals are present, concentration of NO2- increases at the expense of SO42- due to the pH dependence of the reaction:
2 SO2 (aq) + 2 NO2- + H2O -> 2 SO42- + 2 H+ + N2O.
In addition, some of the SO42- precipitates as anhydrite, where calcite dissolution occurs. Negligible amount of O2 is consumed by oxidation of Fe(II) in the water. Calcite dissolution effectively buffers pH that remains close to the pH of 4.6 generated by CO2 dissolution. While the abundance of calcite varies in the formation, calculations with just siderite and K-feldspar result in minimum pH values of 3.4. Thus, the acidification from impurities where calcite is present will not pose a critical problem for the durability of infrastructure or induce reactions that could cause deterioration of the formation strength. However, the impact of impurities on the reservoir properties could scale with the amount of impurities injected, or different injection strategies (i.e., several injection/production cycles, alternating injection of oxidizing/reducing impurities).