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The Sabriyah field located in northern Kuwait primarily produces from the Mauddud and Burgan formations. The upper section of the Burgan formation is referred to as the Sabriyah Upper Burgan (SAUB) reservoir. SAUB reservoir consists of Cretaceous Albian age sandstones and spreads over an area of ~105 km2. This paper sheds light on the successful application of a long-term polymer injectivity (LTPI) test in the SAUB reservoir as a strategic milestone towards phased commercial polymer-flooding development. The main objective of the SAUB LTPI test was to evaluate injectivity at multiple injection rates and polymer concentrations under sub-fracturing conditions. Current EOR efforts target reservoir areas with unfavorable mobility ratio to improve oil recovery and unlock additional oil reserves. The location of the SAUB LTPI test was carefully selected to avoid faults and low channel thickness. Effluent water with TDS ranging from 150,000 to 200,000 ppm was used for polymer solution preparation. Iron content was relatively high (up to 200 ppm) but this was duly mitigated by maintaining low dissolved oxygen levels (i.e. <10 ppb). Fit-for-purpose modular skids were used for water treatment and polymer mixing/injection. A pre-selected sulphonated polymer was used based on extensive lab evaluation to overcome the high TDS, hardness, and temperature of the SAUB reservoir. A step rate test was conducted, and subsurface parting pressure was estimated to be around 5020 psi. Field data indicates that the selected polymer can be injected at commercial rates, under matrix conditions, using treated effluent water without plugging the reservoir. Important polymer rheological properties were generated using field data. Field and lab polymer data were found to be consistent. The LTPI test location average permeability that is lower than that of core plugs used during core-flooding experiments. Consequently, residual resistance factor was increased from a lab derived value of 1.3 to 1.5 based field data. Establishing favorable polymer injectivity under matrix conditions with relatively lower permeability is encouraging because better polymer injectivity is expected in areas having higher permeability. Pre and post polymer injection reservoir modeling were carried out on a sector reservoir model built in CMG STARS utilizing available lab data. Post calibration of the dynamic model was performed using pilot operational and laboratory data, predictive forecasts were then generated to evaluate the techno-commercial feasibility of polymer injection into the SAUB reservoir. Reservoir simulation results based on actual field data demonstrated that polymer-flooding accelerates oil production rates compared to water-flooding. Injecting 0.7 to 0.8 PVI (pore volume injected) at a polymer concentration of 1600 ppm was found to be optimal for commercial polymer-flooding development. The adopted approach and associated results demonstrate the viability of performing customized field trials to fast-track phased commercial polymer-flooding. LTPI test results validated earlier SAUB polymer-flooding forecasts for SAUB polymer-flooding development (SPE paper reference). An incremental oil recovery of 9.6 % can be achieved from polymer-flooding. Polymer-flooding ultimate total cost (UTC) over a period of 10 years was estimated to be 15.80 US$/bbl including the cost of additional wells.
The Sabriyah field located in northern Kuwait primarily produces from the Mauddud and Burgan formations. The upper section of the Burgan formation is referred to as the Sabriyah Upper Burgan (SAUB) reservoir. SAUB reservoir consists of Cretaceous Albian age sandstones and spreads over an area of ~105 km2. This paper sheds light on the successful application of a long-term polymer injectivity (LTPI) test in the SAUB reservoir as a strategic milestone towards phased commercial polymer-flooding development. The main objective of the SAUB LTPI test was to evaluate injectivity at multiple injection rates and polymer concentrations under sub-fracturing conditions. Current EOR efforts target reservoir areas with unfavorable mobility ratio to improve oil recovery and unlock additional oil reserves. The location of the SAUB LTPI test was carefully selected to avoid faults and low channel thickness. Effluent water with TDS ranging from 150,000 to 200,000 ppm was used for polymer solution preparation. Iron content was relatively high (up to 200 ppm) but this was duly mitigated by maintaining low dissolved oxygen levels (i.e. <10 ppb). Fit-for-purpose modular skids were used for water treatment and polymer mixing/injection. A pre-selected sulphonated polymer was used based on extensive lab evaluation to overcome the high TDS, hardness, and temperature of the SAUB reservoir. A step rate test was conducted, and subsurface parting pressure was estimated to be around 5020 psi. Field data indicates that the selected polymer can be injected at commercial rates, under matrix conditions, using treated effluent water without plugging the reservoir. Important polymer rheological properties were generated using field data. Field and lab polymer data were found to be consistent. The LTPI test location average permeability that is lower than that of core plugs used during core-flooding experiments. Consequently, residual resistance factor was increased from a lab derived value of 1.3 to 1.5 based field data. Establishing favorable polymer injectivity under matrix conditions with relatively lower permeability is encouraging because better polymer injectivity is expected in areas having higher permeability. Pre and post polymer injection reservoir modeling were carried out on a sector reservoir model built in CMG STARS utilizing available lab data. Post calibration of the dynamic model was performed using pilot operational and laboratory data, predictive forecasts were then generated to evaluate the techno-commercial feasibility of polymer injection into the SAUB reservoir. Reservoir simulation results based on actual field data demonstrated that polymer-flooding accelerates oil production rates compared to water-flooding. Injecting 0.7 to 0.8 PVI (pore volume injected) at a polymer concentration of 1600 ppm was found to be optimal for commercial polymer-flooding development. The adopted approach and associated results demonstrate the viability of performing customized field trials to fast-track phased commercial polymer-flooding. LTPI test results validated earlier SAUB polymer-flooding forecasts for SAUB polymer-flooding development (SPE paper reference). An incremental oil recovery of 9.6 % can be achieved from polymer-flooding. Polymer-flooding ultimate total cost (UTC) over a period of 10 years was estimated to be 15.80 US$/bbl including the cost of additional wells.
A significant portion of the world's oil reserves are trapped in carbonate reservoirs, many of which are located in the Middle East. Polymer EOR in the carbonate reservoirs tends to be challenging due to limited injectivity and reservoir heterogeneity. This paper presents field results of a successful polymer EOR pilot in the Umm Gudair Minagish Oolite (UGMO) reservoir using treated effluent water at a salinity of up to 257,000 ppm and a reservoir temperature of 72°C. A suitable polymer was identified for UGMO polymer EOR based on extensive laboratory evaluation. Work was then geared towards the implementation of a pilot, mainly to de-risk polymer injectivity using an injector and an offsetting producer located nearly ~87m away. Before starting the pilot operations, a representative sector reservoir model was extracted, history-matched and calibrated using available data to design the envisaged pilot. Thereafter, pilot operations were carried out to generate reliable data using a fit-for-purpose surveillance program and surface facility. The acquired field data were then used to calibrate a high-resolution reservoir simulation model that was used for techno-economic optimization. Based on actual field data, it was observed that polymer injectivity far exceeded original simulation-based expectations. Field operations indicated limited polymer dissolution time, in the range of 1 to 2 hours, despite the extremely high-salinity effluent water that was used. Injected polymer concentration was progressively increased, reaching 2,500 ppm and a surface viscosity of 17 cP, at an injection rate of 3,500 BPD, while staying below the pre-defined maximum allowable injection pressure. Polymer breakthrough was detected at the nearest producer after approximately 3 months of polymer injection, thus indicating favourable sweep efficiency. Resistance factors were found to be more responsive to variations in injection rates as opposed to polymer concentrations as evident from downhole pressure data. Calculated in-situ viscosities were within the expected range and the injected polymer solution demonstrated non-Newtonian pseudo-plastic behavior in line with previously acquired lab data. Based on downhole pressure data, polymer injection was maintained under matrix conditions with no evidence of induced fractures. High-resolution reservoir simulation results indicate promising techno-economic results in terms of oil recovery and cost, thus indicated the feasibility of achieving a Unit-Technical-Cost (UTC) of approximately $20.5/incremental barrel of oil over a waterflood infill case. This paper sheds light on the feasibility of polymer-flooding for a deep carbonate reservoir, using extremely high-salinity effluent water, at a reservoir temperature of 72°C. Techno-economic evaluation of field results is promising. Work is in progress to pave the way for UGMO phased commercial polymer-flooding development on a fast-track basis.
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