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EOR in Fractured Carbonate Reservoirs – low salinity low temperature conditions By Aparna Raju Sagi, Maura C. Puerto, Clarence A. Miller, George J. Hirasaki Rice University Mehdi Salehi, Charles Thomas TIORCO April 26, 2011
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Outline EOR strategy for fractured reservoirs Evaluation at room temperature (~25 °C) o Phase behavior studies – surfactant selection o Viscosity measurements o Imbibition experiments o Adsorption experiments Evaluation at 30 °C and live oil o Phase behavior experiments o Imbibition experiements Conclusions 2
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3 EOR strategy
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Reservoir description o Fractures – high permeability paths o Oil wet – oil trapped in matrix by capillarity o Dolomite, low salinity, 30 °C Recover oil from matrix spontaneous imbibition o IFT reduction Surfactants o Wettability alteration Surfactants Alkali EOR strategy 4 Ref: Hirasaki et. al, 2003
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Current focus – IFT reduction – surfactant flood Surfactant flood desirable characteristics o Low IFT (order of 10 -2 mN/m) o Surfactant-oil-brine phase behavior stays under- optimum o Low adsorption on reservoir rock (chemical cost) o Avoid generation of viscous phases o Tolerance to divalent ions o Solubility in injection and reservoir brine o Easy separation of oil from produced emulsion 5
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6 Phase behavior studies at ~ 25 °C
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Parameter Salinity Surfactant blend ratio Soap/surfactant ratio Optimal parameter Winsor Type - I Winsor Type - II Varying parameter Winsor Type - III micro Procedure 7 Pipette (bottom sealed) Brine + surfactant Oil Initial interface Seal open end 24 hr
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Phase behavior, IFT, solubilization parameter 8 Reed et al. 1977 Salinity, wt% NaCl IFT, mN/m Solubilization parameter momw Vo/Vs Vw/Vs middle upper lower
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Phase behavior Purpose of phase behavior studies o Determine optimal salinity, Cø transition from Winsor Type I to Winsor Type II o Calculate solubilization ratio, Vo/Vs and Vw/Vs o Detect viscous emulsions (undesirable) Parameters o Salinity – 11,000 ppm (incl Ca, Mg) o Surfactant type, Blend ratio (2 surfactants) o Oil type – dead oil vs. live oil o Water oil ratio (WOR) o Surfactant concentration 9
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4wt% 1 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 Brine2 S13D Salinity scan (Multiples of Brine2) WOR ~ 1 0.5wt% 0.25wt% optimal salinity Vo/Vs~ 10 at reservoir salinity 10
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11 Viscosity studies at ~ 25 °C
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Viscosities of phases – function of salinity 12 0.84 0.94 1.05 1.15 1.26 1.36 1.47 Multiples of Brine 2 Optimal salinity reservoir salinity optimal salinity Oil 0.5 wt% S13D
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13 Imbibition studies at ~ 25 °C
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Imbibition results – S13D reservoir cores (1”) 14 S13D 0.5wt% 126md S13D 0.25wt% 151md Mehdi Salehi, TIORCO
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S13D candidate for EOR o under-optimum at reservoir salinity o stays under-optimum upon dilution o Vo/Vs~10 (at 4wt% surfactant concentration) indicative of low IFT o No high viscosity phases at reservoir salinity o ~ 70% recovery in imbibition tests 15
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16 Adsorption studies at ~ 25 °C
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Dynamic adsorption – procedure Sand pack o Limestone sand ~ 20-40 mesh o Washed to remove fines & dried in oven Core holder o Core cleaned with Toluene, THF, Chloroform, methanol o Core holder with 400 – 800psi overburden pressure Vacuum saturation (~ -27 to -29 in Hg) o measure pore volume Permeability measurement 17
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Dynamic adsorption - setup 18 Sample collection Bromide concentration reading Bromide electrode Pressure transducer Pressure monitoring Core holder/ Sand pack Syringe pump/ ISCO pump
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Limestone sandpack ~ 102D Injection solution: Brine 2 with 1000ppm Br - + 0.5wt% S13D Flow rate: 12.24ml/h Pore volume: 72 ml, Time for 1PV ~ 6hrs 19 1PV =.38 ft 3 /ft 2 Lag ~ 0.14 PV Adsorption 0.26 mg/g sand 0.12 mg/g reservoir rock 1PV2PV
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Reservoir core – 6mD 20 Injection solution: Brine 2 with 1000ppm Br - + 0.5wt% S13D Flow rate: 2ml/h Pore volume: ~12 ml, Time for 1PV ~ 6hrs 1PV =.035 ft 3 /ft 2 Effective pore size = 26.8 m Lag ~ 0.54PV to 1.25PV Adsorption 0.12 mg/g rock to 0.28 mg/g rock 3PV4PV day 1day 3 2PV1PV
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Reservoir core – 6mD plugging 21 Expected pressure drop @ 15ml/hr Expected pressure drop @ 2ml/hr Absence of surfactant Presence of surfactant – dyn ads exp day 1 day 11day 3 – no data 1PV2PV3PV4PV5PV
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By Yu Bian diff in area ~ 21 % 3PV4PV day 1day 3 2PV1PV HPLC sample HPLC analysis of effluent 22 3PV4PV2PV1PV
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Reservoir core – 15mD 23 2 micron filter @ inlet – pressure monitored Injection solution: Brine 2 with 1000ppm Br - + 0.5wt% S13D Flow rate: 1ml/h, Pore volume: ~30 ml, Time for 1PV ~ 1.25 days 1PV =.103 ft 3 /ft 2 Effective pore size = 11.8 m Lag ~ 0.67PV Adsorption 0.29 mg/g rock Surfactant Pressure Bromide 1PV2PV3PV4PV5PV day1 2346789 10141516 HPLC sample
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HPLC analysis of effluent 24 diff in area ~ 25 % By Yu Bian
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Adsorption results comparison 25 ExperimentMaterialEquivalent adsorption on reservoir rock (mg/g) Residence time (hrs) DynamicLimestone sand0.126 DynamicDolomite core 6mD 0.12 – 0.286 - overnight DynamicDolomite core 15mD 0.2930 Static (by Yu Bian) Dolomite powder0.3424
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26 Phase behavior studies at ~ 30 °C
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S13D phase behavior 27 S13D 1wt% @ 25 °C Type I microemulsion S13D 1wt% @ 30 °C Type II microemulsion S13D 1wt% @ 30 °C with live oil (600 psi) Type II microemulsion
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S13D/S13B blend scan 30°C 28 10/0 9/1 8/2 7/3 6/4 5/5 4/6 3/7 2/8 1/9 0/10 S13D S13D/S13B ratio S13B Brine 2 salinity;2 wt% aq; WOR = 1 Optimal blend
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29 543210543210 S13D 10 9 8 7 6 5 4 3 2 1 0 S13B 0 1 2 3 4 5 6 7 8 9 10 543210543210 % C s °C 50 40 30 20 10 0 S13D 10 9 8 7 6 5 4 3 2 1 0 S13B 0 1 2 3 4 5 6 7 8 9 10 50 40 30 20 10 0 Phase behavior S13D/S13B blend With dead oil @ 30 °C Aqueous stability test of S13D/S13B blend
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S13D/S13B (70/30) – dead vs live crude @ 30 ° C 30 Dead oil – UNDER-OPTIMUMLive oil – OVER-OPTIMUM After mixing & settling for 1 day Before mixing After mixing & settling for 1 day
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31 Imbibition studies at ~ 30 °C
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Imbibition results –reservoir cores (1”) 32 S13D 0.5wt% 126mD, 25 °C S13D 0.25wt% 151mD 25 °C Mehdi Salehi, TIORCO S13D/S13B 70/30 1wt% 575mD, 30 °C S13D/S13B 60/40 1wt% 221mD, 30 °C
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33 Conclusions
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Dynamic adsorption experiments (absence of oil) o Effluent surfactant concentration plateaus at ~80% injected concentration o Higher PO components are deficient in the effluent sample (in plateau region) o Increase in pressure drop with volume throughput Sensitivity of phase behavior to temperature and oil (dead vs. live) S13D/S13B 70/30 @ 30 °C performance poor compared to S13D @ 25 °C 34
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35 Questions
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36 Back up slides
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S13D surfactant flood – additional experiments Analysis of plugging behavior o HPLC analysis of dynamic adsorption effluent samples – determine missing components o Determine pore size distribution of Yates core samples by NMR and Mercury porosimetry for cores of different permeability o Determine surfactant micelle size o Presence of anhydrite – measure Ca 2+ concentration in dynamic adsorption effluent by ICP Quantify effect of S13D on o wettability – calcite slab contact angle measurements o IFT – spinning drop measurements 37
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NI blend - 4:1 N67-7PO : IOS 15-18 * N67-7PO – Neodol C16-17 7Propoxy Sulfate IOS 15-18 – C15-18 Internal Olefin Sulfonate Optimal salinity ~ 5% NaCl + 1% Na 2 CO 3 Na 2 CO 3 o Generation of soap optimal salinity function of soap to surfactant ratio o Wettability alteration o Reduced adsorption 38 * Liu et.al 2008 (SPE99744)
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NI blend Unsuitable conditions for Alkali Surfactant flooding o Presence of divalent ions in injection fluid Precipitation of CaCO 3 in presence of Na 2 CO 3 o Presence of 600 psi CO 2 Na 2 CO 3 NaHCO 3 lower pH Low pH – no soap generation 39
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N67- 7PO and IOS 20-24 IOS 20-24 – C20-24 Internal Olefin Sulfonate o More lipophilic than IOS 15-18 o reduce optimal salinity Salinity scan – NaCl brine, WOR=1 Blend scan at 3% NaCl salinity, 2wt% surfactant o Optimal blend ratio between 1:4(N:I) - IOS 40 NI blend optimal salinity 5% NaCl + 1% Na 2 CO 3 N67: IOS concentration (aqueous) optimal salinity % NaCl 4:11wt%4 - 4.5 N67: IOS concentration (aqueous) optimal salinity % NaCl 4:11wt%4 - 4.5 1:12wt%, 4wt%3.5 - 4
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41 Salinity scanBlend scan NI 20-24 (4:1 blend) 1 wt% aq NI 20-24 (1:1 blend) 2 wt% aq 3% NaCl salinity 2 wt% aq
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IOS 2024N67-7PO 42
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43 Replacing IOS15-18 with IOS 20-24 reduces optimal salinity Not sufficient to reduce optimal salinity to reservoir salinity
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