add a version of the SPE-1 problem that tests the thermal features of OPM
don't try to feed this to Eclipse, though...
This commit is contained in:
Andreas Lauser
parent
2c8e9ae71b
commit
af09d6e278
16
spe1_thermal/README
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16
spe1_thermal/README
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@ -0,0 +1,16 @@
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This directory contains the input data file for a version of the SPE-1
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[1] problem which has been modified to include thermal effects. The
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intention of it is to test the "pseudo-thermal" features of the OPM
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simulators. For this reason, the dataset will probably produce errors
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or incorrect results if using an ECLiPSE simulator.
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The ownership of the copyright of this dataset is unclear: Some parts
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seem to be written by Schlumberger [2], which in turn seem to be
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modified by Jon Kleppe of NTNU [3] and some (mainly saturation
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function related) data seems to be calculated by SINTEF using MRST.
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Finally some modifications where done by Ove Savareid and Andreas
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Lauser in the context of the OPM project.
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[1] http://www.spe.org/web/csp/datasets/set01.htm
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[2] http://slb.com
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[3] http://www.ipt.ntnu.no/~kleppe/TPG4160/ex3/ODEH.DATA
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592
spe1_thermal/SPE1_THERMAL.DATA
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592
spe1_thermal/SPE1_THERMAL.DATA
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-- =====================================================================
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-- THIS IS THE FIRST SPE COMPARISON PROBLEM,"COMPARISON OF SOLUTIONS TO A
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-- THREE-DIMENSIONAL BLACK-OIL RESERVOIR SIMULATION PROBLEM", REPORTED
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-- BY AZIS AND ODEH AT THE SPE SYMPOSIUM ON RESERVOIR SIMULATION ,
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-- JANUARY 1981. IT IS A NON SWELLING AND SWELLING STUDY. A REGULAR
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-- GRID WITH TWO WELLS (INJECTOR AND PRODUCER)AND A IMPES SOLUTION METHOD
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-- IS USED FOR THIS SIMULATION.THE PRODUCTION IS CONTROLLED BY FLOW RATE
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-- AND MIN. BHP. OIL RATE, GOR, PRESSURE AND GAS SATURATION ARE TO BE REPORTED.
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-- =====================================================================
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RUNSPEC
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-- TITLE
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-- ODEH PROBLEM - IMPLICIT OPTION - 1200 DAYS /
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DIMENS
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10 10 3 /
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NONNC
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OIL
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WATER
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GAS
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DISGAS
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FIELD
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EQLDIMS
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1 100 10 1 1 /
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TABDIMS
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1 1 17 12 1 12 /
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WELLDIMS
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2 1 1 2 /
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NUPCOL
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4 /
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START
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19 'OCT' 1982 /
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NSTACK
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24 /
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--FMTOUT
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--FMTIN
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UNIFOUT
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UNIFIN
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--NOSIM
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--IMPES
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-------------------------------------------------
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-- Thermal stuff in the RUNSPEC section
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-------------------------------------------------
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-- enable the "temperature option"
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TEMP
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-- tell the simulator that we have two hydrocarbon components, oil
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-- (first component) and gas (second)
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COMPS
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2 /
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OCOMPIDX
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1 /
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GCOMPIDX
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2 /
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GRID ================================================================
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-------- IN THIS SECTION , THE GEOMETRY OF THE SIMULATION GRID AND THE
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-------- ROCK PERMEABILITIES AND POROSITIES ARE DEFINED.
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------------------------------------------------------------------------
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-- THE X AND Y DIRECTION CELL SIZES ( DX, DY ) AND THE POROSITIES ARE
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-- CONSTANT THROUGHOUT THE GRID. THESE ARE SET IN THE FIRST 3 LINES
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-- AFTER THE EQUALS KEYWORD. THE CELL THICKNESSES ( DZ ) AND
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-- PERMEABILITES ARE THEN SET FOR EACH LAYER. THE CELL TOP DEPTHS
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-- ( TOPS ) ARE NEEDED ONLY IN THE TOP LAYER ( THOUGH THEY COULD BE.
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-- SET THROUGHOUT THE GRID ). THE SPECIFIED MULTZ VALUES ACT AS
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-- MULTIPLIERS ON THE TRANSMISSIBILITIES BETWEEN THE CURRENT LAYER
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-- AND THE LAYER BELOW.
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DXV
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10*1000.0
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/
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DYV
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10*1000.0
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/
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DZ
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100*20.0 100*30.0 100*50.0
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/
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PORO
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300*0.3
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/
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PERMX
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100*500.0
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100*50.0
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100*200.0
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/
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PERMY
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100*500.0
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100*50.0
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100*200.0
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/
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-- Note: ignoring MULTZ!
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-- layer 1-2 'MULTZ' 0.64 /
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-- layer 2-3 'MULTZ' 0.265625 /
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-- Reducing PERMZ a little instead
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PERMZ
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100*300.0
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100*30.0
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100*50.0
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/
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TOPS
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100*8325.0
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/
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INIT
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PROPS ===============================================================
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-------- THE PROPS SECTION DEFINES THE REL. PERMEABILITIES, CAPILLARY
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-------- PRESSURES, AND THE PVT PROPERTIES OF THE RESERVOIR FLUIDS
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----------------------------------------------------------------------
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-- WATER RELATIVE PERMEABILITY AND CAPILLARY PRESSURE ARE TABULATED AS
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-- A FUNCTION OF WATER SATURATION.
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--
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-- Generated with MRST's family_1() function from the original deck.
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-- SWAT KRW KRO PCOW
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SWOF
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0.120000000000000 0 1.000000000000000 0
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0.121000000000000 0.000000011363636 1.000000000000000 0
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0.140000000000000 0.000000227272727 0.997000000000000 0
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0.170000000000000 0.000000568181818 0.980000000000000 0
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0.240000000000000 0.000001363636364 0.700000000000000 0
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0.319999999000000 0.000002272727261 0.350000004375000 0
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0.370000000000000 0.000002840909091 0.200000000000000 0
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0.420000000000000 0.000003409090909 0.090000000000000 0
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0.520000000000000 0.000004545454545 0.021000000000000 0
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0.570000000000000 0.000005113636364 0.010000000000000 0
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0.620000000000000 0.000005681818182 0.001000000000000 0
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0.720000000000000 0.000006818181818 0.000100000000000 0
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0.820000000000000 0.000007954545455 0.000000000000000 0
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1.000000000000000 0.000010000000000 0 0
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/
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SGOF
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0 0 1.000000000000000 0
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0.001000000000000 0 1.000000000000000 0
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0.020000000000000 0 0.997000000000000 0
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0.050000000000000 0.005000000000000 0.980000000000000 0
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0.120000000000000 0.025000000000000 0.700000000000000 0
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0.199999999000000 0.074999999375000 0.350000004375000 0
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0.200001100000000 0.075000000000000 0.350000000000000 0
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0.250000000000000 0.125000000000000 0.200000000000000 0
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0.300000000000000 0.190000000000000 0.090000000000000 0
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0.400000000000000 0.410000000000000 0.021000000000000 0
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0.449999999000000 0.599999996200000 0.010000000220000 0
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0.450001100000000 0.600000000000000 0.010000000000000 0
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0.500000000000000 0.720000000000000 0.001000000000000 0
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0.600000000000000 0.870000000000000 0.000100000000000 0
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0.700000000000000 0.940000000000000 0 0
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0.850000000000000 0.980000000000000 0 0
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0.880000000000000 0.984000000000000 0 0
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/
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-- PVT PROPERTIES OF WATER
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--
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-- REF. PRES. REF. FVF COMPRESSIBILITY REF VISCOSITY VISCOSIBILITY
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PVTW
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4014.7 1.029 3.13E-6 0.31 0 /
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-- ROCK COMPRESSIBILITY
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--
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-- REF. PRES COMPRESSIBILITY
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ROCK
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14.7 3.0E-6 /
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-- SURFACE DENSITIES OF RESERVOIR FLUIDS
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--
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-- OIL WATER GAS
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DENSITY
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49.1 64.79 0.06054 /
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-- PVT PROPERTIES OF DRY GAS (NO VAPOURISED OIL)
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-- WE WOULD USE PVTG TO SPECIFY THE PROPERTIES OF WET GAS
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--
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-- PGAS BGAS VISGAS
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PVDG
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14.7 166.666 0.008
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264.7 12.093 0.0096
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514.7 6.274 0.0112
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1014.7 3.197 0.014
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2014.7 1.614 0.0189
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2514.7 1.294 0.0208
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3014.7 1.080 0.0228
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4014.7 0.811 0.0268
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5014.7 0.649 0.0309
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9014.7 0.386 0.047 /
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-- PVT PROPERTIES OF LIVE OIL (WITH DISSOLVED GAS)
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-- WE WOULD USE PVDO TO SPECIFY THE PROPERTIES OF DEAD OIL
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--
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-- FOR EACH VALUE OF RS THE SATURATION PRESSURE, FVF AND VISCOSITY
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-- ARE SPECIFIED. FOR RS=1.27 AND 1.618, THE FVF AND VISCOSITY OF
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-- UNDERSATURATED OIL ARE DEFINED AS A FUNCTION OF PRESSURE. DATA
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-- FOR UNDERSATURATED OIL MAY BE SUPPLIED FOR ANY RS, BUT MUST BE
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-- SUPPLIED FOR THE HIGHEST RS (1.618).
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--
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-- RS POIL FVFO VISO
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-- PVTO
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-- 0.001 14.7 1.062 1.04 /
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-- 0.0905 264.7 1.15 0.975 /
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-- 0.18 514.7 1.207 0.91 /
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-- 0.371 1014.7 1.295 0.83 /
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-- 0.636 2014.7 1.435 0.695 /
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-- 0.775 2514.7 1.5 0.641 /
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-- 0.93 3014.7 1.565 0.594 /
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-- 1.270 4014.7 1.695 0.51
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-- 5014.7 1.671 0.549
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-- 9014.7 1.579 0.74 /
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-- 1.618 5014.7 1.827 0.449
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-- 9014.7 1.726 0.605 /
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-- /
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PVTO
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1.0000000000e-03
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1.4700000000e+01 1.0620000000e+00 1.0400000000e+00
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1.0147000000e+03 1.0469628319e+00 1.1195294118e+00
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5.0147000000e+03 9.8932035398e-01 1.5090196078e+00
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/
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9.0500000000e-02
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2.6470000000e+02 1.1500000000e+00 9.7500000000e-01
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1.2647000000e+03 1.1337168142e+00 1.0495588235e+00
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5.2647000000e+03 1.0712979351e+00 1.4147058824e+00
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/
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1.8000000000e-01
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5.1470000000e+02 1.2070000000e+00 9.1000000000e-01
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1.5147000000e+03 1.1899097345e+00 9.7958823529e-01
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5.5147000000e+03 1.1243970501e+00 1.3203921569e+00
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/
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3.7100000000e-01
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1.0147000000e+03 1.2950000000e+00 8.3000000000e-01
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2.0147000000e+03 1.2766637168e+00 8.9347058824e-01
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6.0147000000e+03 1.2063746313e+00 1.2043137255e+00
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/
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6.3600000000e-01
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2.0147000000e+03 1.4350000000e+00 6.9500000000e-01
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3.0147000000e+03 1.4146814159e+00 7.4814705882e-01
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7.0147000000e+03 1.3367935103e+00 1.0084313725e+00
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/
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7.7500000000e-01
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2.5147000000e+03 1.5000000000e+00 6.4100000000e-01
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3.5147000000e+03 1.4787610619e+00 6.9001764706e-01
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7.5147000000e+03 1.3973451327e+00 9.3007843137e-01
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/
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9.3000000000e-01
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3.0147000000e+03 1.5650000000e+00 5.9400000000e-01
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4.0147000000e+03 1.5428407080e+00 6.3942352941e-01
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8.0147000000e+03 1.4578967552e+00 8.6188235294e-01
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/
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1.2700000000e+00
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4.0147000000e+03 1.6950000000e+00 5.1000000000e-01
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5.0147000000e+03 1.6710000000e+00 5.4900000000e-01
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9.0147000000e+03 1.5790000000e+00 7.4000000000e-01
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/
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1.6180000000e+00
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5.0147000000e+03 1.8270000000e+00 4.4900000000e-01
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||||
9.0147000000e+03 1.7260000000e+00 6.0500000000e-01
|
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/
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/
|
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|
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-- OUTPUT CONTROLS FOR PROPS DATA
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-- ACTIVATED FOR SOF3, SWFN, SGFN, PVTW, PVDG, DENSITY AND ROCK KEYWORDS
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RPTPROPS
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1 1 1 0 1 1 1 1 /
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-------------------------------------------------
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-- Thermal stuff in the PROPS section
|
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-------------------------------------------------
|
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|
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-- compressibility of the components in the oil phase
|
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CREF
|
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-- c^O_g c^G_g
|
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1e-6 0 /
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|
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-- the reservoir reference temperature
|
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TREF
|
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-- T^O T^G
|
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554.67 554.67 /
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|
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-- the reservoir reference pressure
|
||||
PREF
|
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-- p^O p^G
|
||||
4790.0 4790.0 /
|
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|
||||
-- temperature dependence of the water density
|
||||
WATDENT
|
||||
-- Tref c_cT1 c_cT2
|
||||
554.67 1* 1* /
|
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|
||||
-- temperature dependence of the oil density
|
||||
THERMEX1
|
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-- c_T1oil c_T1gas
|
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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 ================================================================
|
||||
Loading…
Reference in New Issue
Block a user