! CCS in depleted gas reservoir case SIMULATION SIMULATION_TYPE SUBSURFACE PROCESS_MODELS SUBSURFACE_FLOW Flow MODE COMP3 OPTIONS ISOTHERMAL RESERVOIR_DEFAULTS / / ! end of subsurface_flow / ! end of process models END !! end simulation block SUBSURFACE #=========================== discretization =================================== GRID TYPE grdecl dep_gas.grdecl END #=========================== times ============================================ TIME START_DATE 1 JAN 2010 FINAL_DATE 1 JAN 2060 INITIAL_TIMESTEP_SIZE 1 d MINIMUM_TIMESTEP_SIZE 1.0D-10 d MAXIMUM_TIMESTEP_SIZE 60 d at 0. d MAXIMUM_TIMESTEP_SIZE 120 d at 30 y END #=========================== output options =================================== OUTPUT MASS_BALANCE_FILE PERIODIC TIMESTEP 1 END ECLIPSE_FILE PERIOD_SUM TIMESTEP 1 DATES 1 JAN 2015 1 JAN 2020 1 JAN 2025 DATES 1 JAN 2030 1 JAN 2035 1 JAN 2040 DATES 1 JAN 2045 1 JAN 2050 1 JAN 2055 1 JAN 2060 WRITE_DENSITY OUTFILE END LINEREPT END #=========================== material properties ============================== MATERIAL_PROPERTY formation ID 1 ROCK_COMPRESSIBILITY 7.25d-5 1/Bar ROCK_REFERENCE_PRESSURE 1.0 Bar CHARACTERISTIC_CURVES ch1 / #=========================== Molecular Diffusion ============================= FLUID_PROPERTY PHASE GAS GAS_DIFFUSION_COEFFICIENT 2.0d-5 / #=========================== saturation functions ============================= CHARACTERISTIC_CURVES ch1 TABLE swfn_table PRESSURE_UNITS Pa SWFN 0.2 0 3.1026 0.25 0.0 1.3120 0.3778 0.0180 0.6943 0.4667 0.0607 0.3378 0.5556 0.1438 0.1241 0.6444 0.2809 0.0344 0.7000 0.4089 0.0034 0.7333 0.4855 0.0007 0.8222 0.7709 0.0 0.9111 1.0 0.0 1.0 1.0 0.0 / END TABLE sgfn_table PRESSURE_UNITS Pa SGFN 0.0 0 0 0.05 0 0 0.0889 0.001 0 0.1778 0.01 0 0.2667 0.03 0 0.3556 0.05 0 0.4445 0.10 0 0.5333 0.20 0 0.6222 0.35 0 0.65 0.39 0 0.7111 0.56 0 0.8 1.0 0 / END / #=========================== EOSs ============================================= EOS WATER SURFACE_DENSITY 995.5 END EOS GAS FORMULA_WEIGHT 16.04d0 SURFACE_DENSITY 1.0995 kg/m^3 PVDG DATA_UNITS ! Metric in the Eclipse sense PRESSURE Bar FVF m^3/m^3 VISCOSITY cP END DATA TEMPERATURE 139.0 1.0135 1.186979 0.0107 34.4738 0.033261 0.0127 68.9476 0.016001 0.0134 82.7371 0.013160 0.0138 103.421 0.010358 0.0145 124.105 0.008535 0.0153 137.895 0.007636 0.0159 158.717 0.006597 0.0170 172.369 0.006190 0.0177 206.843 0.005531 0.0195 241.317 0.005118 0.0214 275.790 0.004840 0.0232 310.264 0.004617 0.0250 330.948 0.004509 0.0261 END !end TEMP block END !endDATA !specify temperature dependency for viscosity END !end PVDG END EOS SOLVENT SURFACE_DENSITY 1.0 kg/m^3 CO2_DATABASE co2_dbase.dat END #=========================== wells ================================== WELL_DATA injs1 RADIUS 0.0762 m CIJK_D 25 25 1 5 WELL_TYPE SOLVENT_INJECTOR BHPL 500 Bar SHUT DATE 1 JAN 2025 OPEN TARG_SSV 5000000 m^3/day DATE 1 JAN 2040 SHUT END WELL_DATA injs2 CIJK_D 25 75 1 5 WELL_TYPE SOLVENT_INJECTOR BHPL 500 Bar SHUT DATE 1 JAN 2025 OPEN TARG_SSV 5000000 m^3/day DATE 1 JAN 2040 SHUT END WELL_DATA injs3 CIJK_D 75 25 1 5 WELL_TYPE SOLVENT_INJECTOR BHPL 500 Bar SHUT DATE 1 JAN 2025 OPEN TARG_SSV 5000000 m^3/day DATE 1 JAN 2040 SHUT END WELL_DATA injs4 CIJK_D 75 75 1 5 WELL_TYPE SOLVENT_INJECTOR BHPL 500 Bar SHUT DATE 1 JAN 2025 OPEN TARG_SSV 5000000 m^3/day DATE 1 JAN 2040 SHUT END WELL_DATA prod1 CIJK_D 1 1 5 10 WELL_TYPE PRODUCER BHPL 50 Bar TARG_GSV 12000000 m^3/day DATE 1 JAN 2025 SHUT END WELL_DATA prod2 CIJK_D 1 100 5 10 WELL_TYPE PRODUCER BHPL 50 Bar TARG_GSV 12000000 m^3/day DATE 1 JAN 2025 SHUT END WELL_DATA prod3 CIJK_D 100 1 5 10 WELL_TYPE PRODUCER BHPL 50 Bar TARG_GSV 12000000 m^3/day DATE 1 JAN 2025 SHUT END WELL_DATA prod4 CIJK_D 100 100 5 10 WELL_TYPE PRODUCER BHPL 50 Bar TARG_GSV 12000000 m^3/day DATE 1 JAN 2025 SHUT END #=========================== EQUILIBRATION ================================== EQUILIBRATION PRESSURE 300 Bar DATUM_D 2500 m WGC_D 2700.0 m PCWG_WGC 0.0 Bar RTEMP 139 C / END_SUBSURFACE