diff --git a/spe1_thermal/README b/spe1_thermal/README new file mode 100644 index 0000000..1d8be87 --- /dev/null +++ b/spe1_thermal/README @@ -0,0 +1,16 @@ +This directory contains the input data file for a version of the SPE-1 +[1] problem which has been modified to include thermal effects. The +intention of it is to test the "pseudo-thermal" features of the OPM +simulators. For this reason, the dataset will probably produce errors +or incorrect results if using an ECLiPSE simulator. + +The ownership of the copyright of this dataset is unclear: Some parts +seem to be written by Schlumberger [2], which in turn seem to be +modified by Jon Kleppe of NTNU [3] and some (mainly saturation +function related) data seems to be calculated by SINTEF using MRST. +Finally some modifications where done by Ove Savareid and Andreas +Lauser in the context of the OPM project. + +[1] http://www.spe.org/web/csp/datasets/set01.htm +[2] http://slb.com +[3] http://www.ipt.ntnu.no/~kleppe/TPG4160/ex3/ODEH.DATA diff --git a/spe1_thermal/SPE1_THERMAL.DATA b/spe1_thermal/SPE1_THERMAL.DATA new file mode 100644 index 0000000..7b48117 --- /dev/null +++ b/spe1_thermal/SPE1_THERMAL.DATA @@ -0,0 +1,592 @@ +-- ===================================================================== +-- THIS IS THE FIRST SPE COMPARISON PROBLEM,"COMPARISON OF SOLUTIONS TO A +-- THREE-DIMENSIONAL BLACK-OIL RESERVOIR SIMULATION PROBLEM", REPORTED +-- BY AZIS AND ODEH AT THE SPE SYMPOSIUM ON RESERVOIR SIMULATION , +-- JANUARY 1981. IT IS A NON SWELLING AND SWELLING STUDY. A REGULAR +-- GRID WITH TWO WELLS (INJECTOR AND PRODUCER)AND A IMPES SOLUTION METHOD +-- IS USED FOR THIS SIMULATION.THE PRODUCTION IS CONTROLLED BY FLOW RATE +-- AND MIN. BHP. OIL RATE, GOR, PRESSURE AND GAS SATURATION ARE TO BE REPORTED. +-- ===================================================================== +RUNSPEC +-- TITLE +-- ODEH PROBLEM - IMPLICIT OPTION - 1200 DAYS / + +DIMENS + 10 10 3 / + +NONNC + +OIL + +WATER + +GAS + +DISGAS + +FIELD + +EQLDIMS + 1 100 10 1 1 / + +TABDIMS + 1 1 17 12 1 12 / + +WELLDIMS + 2 1 1 2 / + +NUPCOL + 4 / + +START + 19 'OCT' 1982 / + +NSTACK + 24 / + +--FMTOUT + +--FMTIN + +UNIFOUT + +UNIFIN + +--NOSIM + +--IMPES + +------------------------------------------------- +-- Thermal stuff in the RUNSPEC section +------------------------------------------------- + +-- enable the "temperature option" +TEMP + +-- tell the simulator that we have two hydrocarbon components, oil +-- (first component) and gas (second) +COMPS +2 / + +OCOMPIDX +1 / + +GCOMPIDX +2 / + +GRID ================================================================ +-------- IN THIS SECTION , THE GEOMETRY OF THE SIMULATION GRID AND THE +-------- ROCK PERMEABILITIES AND POROSITIES ARE DEFINED. +------------------------------------------------------------------------ +-- THE X AND Y DIRECTION CELL SIZES ( DX, DY ) AND THE POROSITIES ARE +-- CONSTANT THROUGHOUT THE GRID. THESE ARE SET IN THE FIRST 3 LINES +-- AFTER THE EQUALS KEYWORD. THE CELL THICKNESSES ( DZ ) AND +-- PERMEABILITES ARE THEN SET FOR EACH LAYER. THE CELL TOP DEPTHS +-- ( TOPS ) ARE NEEDED ONLY IN THE TOP LAYER ( THOUGH THEY COULD BE. +-- SET THROUGHOUT THE GRID ). THE SPECIFIED MULTZ VALUES ACT AS +-- MULTIPLIERS ON THE TRANSMISSIBILITIES BETWEEN THE CURRENT LAYER +-- AND THE LAYER BELOW. + +DXV +10*1000.0 +/ + +DYV +10*1000.0 +/ + +DZ +100*20.0 100*30.0 100*50.0 +/ + +PORO +300*0.3 +/ + +PERMX +100*500.0 +100*50.0 +100*200.0 +/ + +PERMY +100*500.0 +100*50.0 +100*200.0 +/ + +-- Note: ignoring MULTZ! +-- layer 1-2 'MULTZ' 0.64 / +-- layer 2-3 'MULTZ' 0.265625 / +-- Reducing PERMZ a little instead +PERMZ +100*300.0 +100*30.0 +100*50.0 +/ + + +TOPS +100*8325.0 +/ + + +INIT + + +PROPS =============================================================== +-------- THE PROPS SECTION DEFINES THE REL. PERMEABILITIES, CAPILLARY +-------- PRESSURES, AND THE PVT PROPERTIES OF THE RESERVOIR FLUIDS + +---------------------------------------------------------------------- +-- WATER RELATIVE PERMEABILITY AND CAPILLARY PRESSURE ARE TABULATED AS +-- A FUNCTION OF WATER SATURATION. +-- +-- Generated with MRST's family_1() function from the original deck. +-- SWAT KRW KRO PCOW +SWOF + 0.120000000000000 0 1.000000000000000 0 + 0.121000000000000 0.000000011363636 1.000000000000000 0 + 0.140000000000000 0.000000227272727 0.997000000000000 0 + 0.170000000000000 0.000000568181818 0.980000000000000 0 + 0.240000000000000 0.000001363636364 0.700000000000000 0 + 0.319999999000000 0.000002272727261 0.350000004375000 0 + 0.370000000000000 0.000002840909091 0.200000000000000 0 + 0.420000000000000 0.000003409090909 0.090000000000000 0 + 0.520000000000000 0.000004545454545 0.021000000000000 0 + 0.570000000000000 0.000005113636364 0.010000000000000 0 + 0.620000000000000 0.000005681818182 0.001000000000000 0 + 0.720000000000000 0.000006818181818 0.000100000000000 0 + 0.820000000000000 0.000007954545455 0.000000000000000 0 + 1.000000000000000 0.000010000000000 0 0 +/ + + +SGOF + 0 0 1.000000000000000 0 + 0.001000000000000 0 1.000000000000000 0 + 0.020000000000000 0 0.997000000000000 0 + 0.050000000000000 0.005000000000000 0.980000000000000 0 + 0.120000000000000 0.025000000000000 0.700000000000000 0 + 0.199999999000000 0.074999999375000 0.350000004375000 0 + 0.200001100000000 0.075000000000000 0.350000000000000 0 + 0.250000000000000 0.125000000000000 0.200000000000000 0 + 0.300000000000000 0.190000000000000 0.090000000000000 0 + 0.400000000000000 0.410000000000000 0.021000000000000 0 + 0.449999999000000 0.599999996200000 0.010000000220000 0 + 0.450001100000000 0.600000000000000 0.010000000000000 0 + 0.500000000000000 0.720000000000000 0.001000000000000 0 + 0.600000000000000 0.870000000000000 0.000100000000000 0 + 0.700000000000000 0.940000000000000 0 0 + 0.850000000000000 0.980000000000000 0 0 + 0.880000000000000 0.984000000000000 0 0 +/ + +-- PVT PROPERTIES OF WATER +-- +-- REF. PRES. REF. FVF COMPRESSIBILITY REF VISCOSITY VISCOSIBILITY +PVTW + 4014.7 1.029 3.13E-6 0.31 0 / + +-- ROCK COMPRESSIBILITY +-- +-- REF. PRES COMPRESSIBILITY +ROCK + 14.7 3.0E-6 / + +-- SURFACE DENSITIES OF RESERVOIR FLUIDS +-- +-- OIL WATER GAS +DENSITY + 49.1 64.79 0.06054 / + +-- PVT PROPERTIES OF DRY GAS (NO VAPOURISED OIL) +-- WE WOULD USE PVTG TO SPECIFY THE PROPERTIES OF WET GAS +-- +-- PGAS BGAS VISGAS +PVDG + 14.7 166.666 0.008 + 264.7 12.093 0.0096 + 514.7 6.274 0.0112 + 1014.7 3.197 0.014 + 2014.7 1.614 0.0189 + 2514.7 1.294 0.0208 + 3014.7 1.080 0.0228 + 4014.7 0.811 0.0268 + 5014.7 0.649 0.0309 + 9014.7 0.386 0.047 / + +-- PVT PROPERTIES OF LIVE OIL (WITH DISSOLVED GAS) +-- WE WOULD USE PVDO TO SPECIFY THE PROPERTIES OF DEAD OIL +-- +-- FOR EACH VALUE OF RS THE SATURATION PRESSURE, FVF AND VISCOSITY +-- ARE SPECIFIED. FOR RS=1.27 AND 1.618, THE FVF AND VISCOSITY OF +-- UNDERSATURATED OIL ARE DEFINED AS A FUNCTION OF PRESSURE. DATA +-- FOR UNDERSATURATED OIL MAY BE SUPPLIED FOR ANY RS, BUT MUST BE +-- SUPPLIED FOR THE HIGHEST RS (1.618). +-- +-- RS POIL FVFO VISO +-- PVTO +-- 0.001 14.7 1.062 1.04 / +-- 0.0905 264.7 1.15 0.975 / +-- 0.18 514.7 1.207 0.91 / +-- 0.371 1014.7 1.295 0.83 / +-- 0.636 2014.7 1.435 0.695 / +-- 0.775 2514.7 1.5 0.641 / +-- 0.93 3014.7 1.565 0.594 / +-- 1.270 4014.7 1.695 0.51 +-- 5014.7 1.671 0.549 +-- 9014.7 1.579 0.74 / +-- 1.618 5014.7 1.827 0.449 +-- 9014.7 1.726 0.605 / +-- / +PVTO +1.0000000000e-03 +1.4700000000e+01 1.0620000000e+00 1.0400000000e+00 +1.0147000000e+03 1.0469628319e+00 1.1195294118e+00 +5.0147000000e+03 9.8932035398e-01 1.5090196078e+00 +/ +9.0500000000e-02 +2.6470000000e+02 1.1500000000e+00 9.7500000000e-01 +1.2647000000e+03 1.1337168142e+00 1.0495588235e+00 +5.2647000000e+03 1.0712979351e+00 1.4147058824e+00 +/ +1.8000000000e-01 +5.1470000000e+02 1.2070000000e+00 9.1000000000e-01 +1.5147000000e+03 1.1899097345e+00 9.7958823529e-01 +5.5147000000e+03 1.1243970501e+00 1.3203921569e+00 +/ +3.7100000000e-01 +1.0147000000e+03 1.2950000000e+00 8.3000000000e-01 +2.0147000000e+03 1.2766637168e+00 8.9347058824e-01 +6.0147000000e+03 1.2063746313e+00 1.2043137255e+00 +/ +6.3600000000e-01 +2.0147000000e+03 1.4350000000e+00 6.9500000000e-01 +3.0147000000e+03 1.4146814159e+00 7.4814705882e-01 +7.0147000000e+03 1.3367935103e+00 1.0084313725e+00 +/ +7.7500000000e-01 +2.5147000000e+03 1.5000000000e+00 6.4100000000e-01 +3.5147000000e+03 1.4787610619e+00 6.9001764706e-01 +7.5147000000e+03 1.3973451327e+00 9.3007843137e-01 +/ +9.3000000000e-01 +3.0147000000e+03 1.5650000000e+00 5.9400000000e-01 +4.0147000000e+03 1.5428407080e+00 6.3942352941e-01 +8.0147000000e+03 1.4578967552e+00 8.6188235294e-01 +/ +1.2700000000e+00 +4.0147000000e+03 1.6950000000e+00 5.1000000000e-01 +5.0147000000e+03 1.6710000000e+00 5.4900000000e-01 +9.0147000000e+03 1.5790000000e+00 7.4000000000e-01 +/ +1.6180000000e+00 +5.0147000000e+03 1.8270000000e+00 4.4900000000e-01 +9.0147000000e+03 1.7260000000e+00 6.0500000000e-01 +/ +/ + +-- OUTPUT CONTROLS FOR PROPS DATA +-- ACTIVATED FOR SOF3, SWFN, SGFN, PVTW, PVDG, DENSITY AND ROCK KEYWORDS +RPTPROPS +1 1 1 0 1 1 1 1 / + +------------------------------------------------- +-- Thermal stuff in the PROPS section +------------------------------------------------- + +-- compressibility of the components in the oil phase +CREF +-- c^O_g c^G_g + 1e-6 0 / + +-- the reservoir reference temperature +TREF +-- T^O T^G + 554.67 554.67 / + +-- the reservoir reference pressure +PREF +-- p^O p^G + 4790.0 4790.0 / + +-- temperature dependence of the water density +WATDENT +-- Tref c_cT1 c_cT2 + 554.67 1* 1* / + +-- temperature dependence of the oil density +THERMEX1 +-- c_T1oil c_T1gas + 0.0 0.0 / + +-- reference conditions for the viscosity tables +VISCREF +-- p Rs +4790 0.0 / + +-- temperature dependence of the water viscosity +WATVISCT +-- T mu_w + 59.0 0.6 + 95.0 0.31 + 150.0 0.25 / + +-- temperature dependence of the oil viscosity +OILVISCT +-- T mu_o + 59.0 1.7 + 95.0 1.5 + 150.0 1.3 / + +-- temperature dependence of the component viscosity in the gas phase +GASVISCT +-- T mu^O_g mu^G_g + 59.0 0.0 0.0150 + 95.0 0.0 0.0230 + 150.0 0.0 0.0300 / + + +SOLUTION =============================================================== +-------- THE SOLUTION SECTION DEFINES THE INITIAL STATE OF THE SOLUTION +-------- VARIABLES (PHASE PRESSURES, SATURATIONS AND GAS-OIL RATIOS) +------------------------------------------------------------------------ +-- DATA FOR INITIALISING FLUIDS TO POTENTIAL EQUILIBRIUM +-- +-- DATUM DATUM OWC OWC GOC GOC RSVD RVVD SOLN +-- DEPTH PRESS DEPTH PCOW DEPTH PCOG TABLE TABLE METH +-- EQUIL +-- 8400 4800 8500 0 8200 0 1 0 0 / + +-- VARIATION OF INITIAL RS WITH DEPTH +-- +-- DEPTH RS +-- RSVD +-- 8200 1.270 +-- 8500 1.270 / + +-- PRESSURE +-- 100*3.297832774859256e7 +-- 100*3.302313357125603e7 +-- 100*3.309483500720813e7 +-- / +PRESSURE +100*4783.10205078125 +100*4789.60058593750 +100*4800.00000000000 +/ + +SWAT +300*0.12 +/ + +SGAS +300*0.0 +/ + +-- RS +-- 300*226.1966570852417 +-- / +RS +300*1.27 +/ + +-- OUTPUT CONTROLS (SWITCH ON OUTPUT OF INITIAL GRID BLOCK PRESSURES) +RPTSOL + RESTART=2 PRES DENW DENO DENG POIL PGAS PWAT VOIL VGAS VWAT KRO KRG KRW RSSAT / +-- RESTART=2 DENSO DENSG DENSW POIL PGAS PWAR VOIL VGAS VWAT KRO KRG KRW RSSAT / + +------------------------------------------------- +-- Thermal stuff in the SOLUTION section +------------------------------------------------- + +-- set the temperature of the reservoir +EQUALS +TEMPI 95 / +/ + +-- increase the temperature around the injector +BOX +1 3 +1 3 +1 3 +/ + +ADD +TEMPI 50 / +/ + +ENDBOX +/ + +SUMMARY =============================================================== +-------- THIS SECTION SPECIFIES DATA TO BE WRITTEN TO THE SUMMARY FILES +-------- AND WHICH MAY LATER BE USED WITH THE ECLIPSE GRAPHICS PACKAGE +------------------------------------------------------------------------ + +EXCEL + +SEPARATE + +--REQUEST PRINTED OUTPUT OF SUMMARY FILE DATA + +RUNSUM + +-- FIELD OIL PRODUCTION +FOPR + +-- WELL GAS-OIL RATIO FOR PRODUCER +WGOR +-- 'PRODUCER' +/ +-- WELL BOTTOM-HOLE PRESSURE +WBHP +-- 'PRODUCER' +/ + +-- GAS AND OIL SATURATIONS IN INJECTION AND PRODUCTION CELL +BGSAT +10 10 3 / +1 1 1 / +/ +BOSAT +10 10 3 / +1 1 1 / +/ + +-- PRESSURE IN INJECTION AND PRODUCTION CELL +BPR +10 10 3 / +1 1 1 / +/ + +SCHEDULE =============================================================== +-------- THE SCHEDULE SECTION DEFINES THE OPERATIONS TO BE SIMULATED +------------------------------------------------------------------------ +-- CONTROLS ON OUTPUT AT EACH REPORT TIME +RPTSCHED + 1 0 1 1 0 0 4 2 2 0 0 2 0 0 0 + 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 + 0 0 0 0 0 0 0 0 1 0 0 0 0 0 0 / + + +--IMPES +-- 1.0 1.0 10000.0 / + +-- SET 'NO RESOLUTION' OPTION +--DRSDT +-- 0 / + +-- SET INITIAL TIME STEP TO 1 DAY AND MAXIMUM TO 6 MONTHS +TUNING +1 182.5 / +1.0 0.5 1.0E-6 / +/ + +-- WELL SPECIFICATION DATA +-- +-- WELL GROUP LOCATION BHP PI +-- NAME NAME I J DEPTH DEFN +WELSPECS + 'PRODUCER' 'G' 10 10 8400 'OIL' / + 'INJECTOR' 'G' 1 1 8335 'GAS' / +/ + +-- COMPLETION SPECIFICATION DATA +-- +-- WELL -LOCATION- OPEN/ SAT CONN WELL +-- NAME I J K1 K2 SHUT TAB FACT DIAM +COMPDAT + 'PRODUCER' 10 10 3 3 'OPEN' 0 -1 0.5 / + 'INJECTOR' 1 1 1 1 'OPEN' 1 -1 0.5 / + / + +-- PRODUCTION WELL CONTROLS +-- +-- WELL OPEN/ CNTL OIL WATER GAS LIQU RES BHP +-- NAME SHUT MODE RATE RATE RATE RATE RATE +WCONPROD + 'PRODUCER' 'OPEN' 'ORAT' 20000 4* 1000 / + / +-- WCONPROD +-- 'PRODUCER' 'OPEN' 'BHP' 5* 1000 / +-- / + +-- INJECTION WELL CONTROLS +-- +-- WELL INJ OPEN/ CNTL FLOW +-- NAME TYPE SHUT MODE RATE +-- WCONINJ +-- 'INJECTOR' 'GAS' 'OPEN' 'RATE' 100000 / +WCONINJE + 'INJECTOR' 'GAS' 'OPEN' 'RATE' 100000 100000 50000/ + / + +-- YEAR 1 + +TSTEP +--0.2343 0.1393 0.1840 0.2189 0.2235 +--1.0 4.0 2*5.0 6*5.0 10*25.0 +1.0 14.0 13*25.0 + / + +TSTEP + 25.0 + / + +-- YEAR 2 + +TSTEP + 13*20.0 7*13.0 + / + +TSTEP + 14.0 + / + +-- YEAR 3 + +TSTEP + 17*10.0 + / + +TSTEP + 12.5 + / + +-- 912.50 --> 1000.0 + +TSTEP + 8.5 16*5.0 + / + +TSTEP + 5.0 + / + +-- 1000.0 --> 1100.0 + +TSTEP + 19*5.0 + / + +TSTEP + 5.0 + / + +-- 1100.0 --> 1200.0 + +TSTEP + 19*5.0 + / + +TSTEP + 5.0 + / + + +TSTEP +10.0 / + +END ================================================================