add a simplified version of the SPE1 dataset
the only remarkable aspect of this deck is that the current version of the CPR preconditioner in opm-autodiff breaks down: ``` and@heuristix:~/src/opm-autodiff|master > ./bin/sim_fibo_ad deck_filename=../opm-data/simplespe1/SIMPLESPE1.DATA ================ Test program for fully implicit three-phase black-oil flow =============== --------------- Reading parameters --------------- deck_filename found at /, value is ../opm-data/simplespe1/SIMPLESPE1.DATA strict_parsing not found. Using default value 'true'. deck_filename found at /, value is ../opm-data/simplespe1/SIMPLESPE1.DATA output not found. Using default value 'true'. output_interval not found. Using default value '1'. output_dir not found. Using default value '.'. pvt_tab_size not found. Using default value '-1'. sat_tab_size not found. Using default value '-1'. threephase_model not found. Using default value 'gwseg'. use_cpr not found. Using default value 'true'. output not found. Using default value 'true'. output_dir not found. Using default value 'output'. output not found. Using default value 'true'. output_vtk not found. Using default value 'true'. output_dir not found. Using default value 'output'. output_interval not found. Using default value '1'. ================ Starting main simulation loop =============== --------------- Simulation step number 0 --------------- Current time (days) 0 Current stepsize (days) 1 Total time (days) 1216 dp_max_rel not found. Using default value '1e+09'. ds_max not found. Using default value '0.2'. drs_max_rel not found. Using default value '1e+09'. relax_max not found. Using default value '0.5'. max_iter not found. Using default value '15'. relax_type not found. Using default value 'dampen'. Iteration Residual 0 1.29402173 terminate called after throwing an instance of 'Dune::ISTLError' Aborted ``` on the other hand, everything works fine if the CPR preconditioner is not used: ``` and@heuristix:~/src/opm-autodiff|master > ./bin/sim_fibo_ad deck_filename=../opm-data/simplespe1/SIMPLESPE1.DATA use_cpr=false ================ Test program for fully implicit three-phase black-oil flow =============== --------------- Reading parameters --------------- deck_filename found at /, value is ../opm-data/simplespe1/SIMPLESPE1.DATA strict_parsing not found. Using default value 'true'. deck_filename found at /, value is ../opm-data/simplespe1/SIMPLESPE1.DATA output not found. Using default value 'true'. output_interval not found. Using default value '1'. output_dir not found. Using default value '.'. pvt_tab_size not found. Using default value '-1'. sat_tab_size not found. Using default value '-1'. threephase_model not found. Using default value 'gwseg'. use_cpr found at /, value is 'false'. linsolver not found. Using default value 'umfpack'. output not found. Using default value 'true'. output_dir not found. Using default value 'output'. output not found. Using default value 'true'. output_vtk not found. Using default value 'true'. output_dir not found. Using default value 'output'. output_interval not found. Using default value '1'. ================ Starting main simulation loop =============== --------------- Simulation step number 0 --------------- Current time (days) 0 Current stepsize (days) 1 Total time (days) 1216 dp_max_rel not found. Using default value '1e+09'. ds_max not found. Using default value '0.2'. drs_max_rel not found. Using default value '1e+09'. relax_max not found. Using default value '0.5'. max_iter not found. Using default value '15'. relax_type not found. Using default value 'dampen'. Iteration Residual 0 1.29402173 1 0.0614937239 2 1.45760381e-05 Fully implicit solver took: 0.097702 seconds. --------------- Simulation step number 1 --------------- Current time (days) 1 Current stepsize (days) 14 Total time (days) 1216 ... ```
This commit is contained in:
parent
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simplespe1/README
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simplespe1/README
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This directory contains an simple input data file which is based on
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the first comparison project of the society of petroleum engineers
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[1]. The dataset consists of a single file called 'SIMPLESPE1.DATA'
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and uses the ECL format which is used by many standard commercial
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simulators for oil reservoirs.
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The simplifications are that the grid consists only of a single layer
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of cells, and that there is no injector well specified. (i.e., only a
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producer is present.)
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Just like for the SPE1 dataset, the ownership of the copyright of this
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file is unclear: Some parts seem to be written by Schlumberger [2],
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which in turn seem to be modified by Jon Kleppe of NTNU [3] and some
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(mainly saturation function related) data seems to be calculated by
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SINTEF using MRST. Finally some modifications where done by Ove
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Savareid and Andreas 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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simplespe1/SIMPLESPE1.DATA
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simplespe1/SIMPLESPE1.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 1 /
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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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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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DZV
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100.0
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/
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PORO
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100*0.3
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/
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PERMX
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100*500.0
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/
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PERMY
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100*500.0
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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*500.0
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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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SOLUTION ===============================================================
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-------- THE SOLUTION SECTION DEFINES THE INITIAL STATE OF THE SOLUTION
|
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-------- VARIABLES (PHASE PRESSURES, SATURATIONS AND GAS-OIL RATIOS)
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------------------------------------------------------------------------
|
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-- DATA FOR INITIALISING FLUIDS TO POTENTIAL EQUILIBRIUM
|
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--
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-- DATUM DATUM OWC OWC GOC GOC RSVD RVVD SOLN
|
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-- DEPTH PRESS DEPTH PCOW DEPTH PCOG TABLE TABLE METH
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-- EQUIL
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-- 8400 4800 8500 0 8200 0 1 0 0 /
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|
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-- VARIATION OF INITIAL RS WITH DEPTH
|
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--
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-- DEPTH RS
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-- RSVD
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-- 8200 1.270
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-- 8500 1.270 /
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-- PRESSURE
|
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-- 100*3.297832774859256e7
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-- 100*3.302313357125603e7
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-- 100*3.309483500720813e7
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-- /
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PRESSURE
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100*4800.00000000000
|
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/
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SWAT
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100*0.12
|
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/
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|
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SGAS
|
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100*0.0
|
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/
|
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|
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-- RS
|
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-- 300*226.1966570852417
|
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-- /
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RS
|
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100*1.27
|
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/
|
||||
|
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-- OUTPUT CONTROLS (SWITCH ON OUTPUT OF INITIAL GRID BLOCK PRESSURES)
|
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RPTSOL
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RESTART=2 PRES DENW DENO DENG POIL PGAS PWAT VOIL VGAS VWAT KRO KRG KRW RSSAT /
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-- RESTART=2 DENSO DENSG DENSW POIL PGAS PWAR VOIL VGAS VWAT KRO KRG KRW RSSAT /
|
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|
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SUMMARY ===============================================================
|
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-------- THIS SECTION SPECIFIES DATA TO BE WRITTEN TO THE SUMMARY FILES
|
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-------- AND WHICH MAY LATER BE USED WITH THE ECLIPSE GRAPHICS PACKAGE
|
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------------------------------------------------------------------------
|
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|
||||
EXCEL
|
||||
|
||||
SEPARATE
|
||||
|
||||
--REQUEST PRINTED OUTPUT OF SUMMARY FILE DATA
|
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|
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RUNSUM
|
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|
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-- FIELD OIL PRODUCTION
|
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FOPR
|
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|
||||
-- WELL GAS-OIL RATIO FOR PRODUCER
|
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WGOR
|
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-- 'PRODUCER'
|
||||
/
|
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-- WELL BOTTOM-HOLE PRESSURE
|
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WBHP
|
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-- 'PRODUCER'
|
||||
/
|
||||
|
||||
-- GAS AND OIL SATURATIONS IN INJECTION AND PRODUCTION CELL
|
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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' /
|
||||
/
|
||||
|
||||
-- COMPLETION SPECIFICATION DATA
|
||||
--
|
||||
-- WELL -LOCATION- OPEN/ SAT CONN WELL
|
||||
-- NAME I J K1 K2 SHUT TAB FACT DIAM
|
||||
COMPDAT
|
||||
'PRODUCER' 10 10 1 1 'OPEN' 0 -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
|
||||
-- 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