Revert "This commit i contains Bg modififcation : "

This commit is contained in:
Alf Birger Rustad 2016-01-14 19:19:34 +01:00
parent 89af152f0b
commit ef1d79f05c
7 changed files with 10063 additions and 1526350 deletions

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@ -1,7 +1,13 @@
This is the script of the SPE10MODEL1 case.
The SPE paper suggested that Qinj=0.2641 Mscf/d.
Nevertheless it is impossible to get results matching those of the SPE paper.
After few different tries, a value of Qinj=34.61 Mscf/d seems to give staisfying results.
If Qinj=0.2461 Mscf/d, tuning is not necessary
If Qinj=34.61 Mscf/d, the param file should be used for the Flow run.
In previous versio, wrong values of Bg were entered (units problem), correct value is 178.1076.
Qinj=34.61 Mscf/d is the implemented value.
Few changes:
- TABDIMS item 3 has been increased to use only one SGOF table
- PVDO & PVDG contained more constraining data to ensure simulating uncompressible fluids.
- Timestep in the data file is limited to 10 days to avoid convergence issues (50 day timestep do not run on Flow)
- It takes about 1 min to run the simulation on eclipse and about 1 week with Flow
- Timestep in the data file is limited to 10 days to avoid convergence issues
- It takes about 1 min to run the simulation on eclipse and about 1 hour with Flow

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@ -53,8 +53,8 @@ UNIFOUT
START
1 'JAN' 1967 /
--NSTACK
-- 500 /
NSTACK
500 /
@ -183,25 +183,25 @@ PVDO
10000 0.999990 1.000010
/
-- Bg equals to 178.1076 because the fluid is uncompressible (unit: rb/Mscf)
-- Bg equals to 1 because the fluid is uncompressible
-- Eclipse cannot accept 2 identical values of Bg for diff pres.
-- Gas Phase Bg MUg
-- pressure
PVDG
14 178.107600997 0.009999
100 178.107600996 0.010000
1000 178.107600995 0.010001
2000 178.107600994 0.010002
3000 178.107600993 0.010003
4000 178.107600992 0.010004
5000 178.107600991 0.010005
6000 178.107600990 0.010006
7000 178.107600989 0.010007
8000 178.107600988 0.010008
9000 178.107600987 0.010009
10000 178.107600986 0.010010
14 1.000001 0.009999
100 1.000000 0.010000
1000 0.999999 0.010001
2000 0.999998 0.010002
3000 0.999997 0.010003
4000 0.999996 0.010004
5000 0.999995 0.010005
6000 0.999994 0.010006
7000 0.999993 0.010007
8000 0.999992 0.010008
9000 0.999991 0.010009
10000 0.999990 0.010010
/
--REF. PRES COMPRESSIBILITY - TAKEN FROM MODEL 2
@ -250,10 +250,10 @@ SCHEDULE ===================================================
RPTRST
'BASIC=2' /
--TUNING
-- /
-- /
-- 2* 500 /
TUNING
/
/
2* 500 /
WELSPECS

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@ -1,950 +0,0 @@
-- This reservoir simulation is made available under the open Database
-- License: http://opendatacommons.org/licenses/odbl/1.0/
-- Individual contents of the database are licensed under the Database contents
-- License : http://opendatacommons.org/licenses/dbcl/1.0/
-- Copyright (C) 2015 Statoil
-- ===============================================================================
-- SPE 10 - MODEL 1
-- Simulation based on the followinf SPE paper:
-- "Tenth SPE comparative solution project: a comparison of upscaling techniques"
-- By Mike Christie (Heriot-Wat University) and Martin Blunt (Imperial College)
-- SPE, August 2001
-- ===============================================================================
RUNSPEC
TITLE
SPE10:TENTH SPE COMPARATIVE SOLUTION PROJECT: A COMPARISON OF UPSCALING TECHNIQUES - MODEL 1
DIMENS
100 1 20 /
NONNC
OIL
WATER
GAS
FIELD
EQLDIMS
3* /
TABDIMS
2* 50 /
WELLDIMS
2 20 1 2 /
UNIFOUT
START
1 'JAN' 1967 /
NSTACK
500 /
-- =================================================
------- In this section, the geometry of the simulation
------- grid and the rock perøeabilities, porosities are
------- defined.
-- =================================================
GRID
NOECHO
INIT
INCLUDE
'SPE10MODEL1.GRDECL' /
PORO
2000*0.2 /
INCLUDE
PERM_SPE10MODEL1.INC
/
ECHO
-- ========================================================================
PROPS
-- Sg Krg Kro Pcgo
SGOF
0.000000 0 1.000000 0.000000
0.025000 0 0.912530 0.000000
0.050000 0 0.830041 0.000000
0.075000 0 0.752410 0.000000
0.100000 0.000001 0.679518 0.000000
0.125000 0.000007 0.611238 0.000000
0.150000 0.000031 0.547448 0.000000
0.175000 0.000093 0.488020 0.000000
0.200000 0.000232 0.432827 0.000000
0.225000 0.000501 0.381737 0.000000
0.250000 0.000977 0.334621 0.000000
0.275000 0.001760 0.291345 0.000000
0.300000 0.002980 0.251773 0.000000
0.325000 0.004800 0.215767 0.000000
0.350000 0.007416 0.183188 0.000000
0.375000 0.011065 0.153893 0.000000
0.400000 0.016028 0.127737 0.000000
0.425000 0.022631 0.104573 0.000000
0.450000 0.031250 0.084248 0.000000
0.475000 0.042315 0.066609 0.000000
0.500000 0.056314 0.051496 0.000000
0.525000 0.073794 0.038746 0.000000
0.550000 0.095367 0.028191 0.000000
0.575000 0.121716 0.019658 0.000000
0.600000 0.153590 0.012965 0.000000
0.625000 0.191818 0.007925 0.000000
0.650000 0.237305 0.004338 0.000000
0.675000 0.291038 0.001995 0.000000
0.700000 0.354093 0.000668 0.000000
0.725000 0.427631 0.000103 0.000000
0.750000 0.512909 0.000000 0.000000
0.775000 0.611280 0.000000 0.000000
0.800000 0.724196 0.000000 0.000000
0.825000 0.853215 0.000000 0.000000
0.85 1 0 0
1 1 0 0 /
-- No water in the reservoir but Flow is a 3-phase simulator so water
-- is placed below the reservoir and has no impact on simulation
--Sw Krw Kro Pcgo
SWOF
0 0 1 0
0.200 0.0001 0.9999 0
0.250 0.0069 0.8403 0
0.300 0.0278 0.6944 0
0.350 0.0625 0.5625 0
0.400 0.1111 0.4444 0
0.450 0.1736 0.3403 0
0.500 0.2500 0.2500 0
0.550 0.3403 0.1736 0
0.600 0.4444 0.1111 0
0.650 0.5625 0.0625 0
0.700 0.6944 0.0278 0
0.750 0.8403 0.0069 0
0.800 1.0000 0.0000 0 /
-- Oil Dens Wat Dens Gas Dens
DENSITY
43.68 62.430 0.0624
/
-- NO WATER, BUT NEEDED FOR FLOW, TAKEN FROM MODEL2
-- REF PRES Bw WAT.COMP WAT.VISC
PVTW
6000 1 0.000003 0.3 /
-- Bo equals to one, fuids are uncompressible
-- Eclipse do not accept 2 identical Bo for diff pres.
-- Oil Pres Bo MUo
PVDO
14 1.000001 0.999999
100 1.000000 1.000000
1000 0.999999 1.000001
2000 0.999998 1.000002
3000 0.999997 1.000003
4000 0.999996 1.000004
5000 0.999995 1.000005
6000 0.999994 1.000006
7000 0.999993 1.000007
8000 0.999992 1.000008
9000 0.999991 1.000009
10000 0.999990 1.000010
/
-- Bg equals to 1 because the fluid is uncompressible, in field unit Bg equals 178
-- Eclipse cannot accept 2 identical values of Bg for diff pres.
-- Gas Phase Bg MUg
-- pressure
PVDG
14 178.107600997 0.009999
100 178.107600996 0.010000
1000 178.107600995 0.010001
2000 178.107600994 0.010002
3000 178.107600993 0.010003
4000 178.107600992 0.010004
5000 178.107600991 0.010005
6000 178.107600990 0.010006
7000 178.107600989 0.010007
8000 178.107600988 0.010008
9000 178.107600987 0.010009
10000 178.107600986 0.010010
/
--REF. PRES COMPRESSIBILITY - TAKEN FROM MODEL 2
ROCK
6000 0.000001
/
SOLUTION ==================================================
-- Datum Pres WOC Pcwoc GOC Pcgoc
EQUIL
0 100 50 0 0 0 2* 0 /
SUMMARY ===================================================
RUNSUM
FOPT
FGPT
FOPR
FGPR
FGIR
FGIT
FPR
FGIR
WBHP
'INJ'
'PROD'
/
WPI
'INJ'
'PROD'
/
WOPR
/
WGIR
/
WGPR
/
SCHEDULE ===================================================
RPTRST
'BASIC=2' /
TUNING
/
/
2* 500 1* 25 /
WELSPECS
'INJ' G1 1 1 1.25 GAS /
'PROD' G1 100 1 1.25 OIL /
/
COMPDAT
'INJ' 1 1 1 20 OPEN 2* 2 /
'PROD' 100 1 1 20 OPEN 2* 2 /
/
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
WCONINJE
'INJ' GAS OPEN RESV 1* 43.839979 10000000 /
/
TSTEP
323*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
5*10 /
WCONPROD
'PROD' OPEN BHP 5* 100 /
/
TSTEP
50 /
WCONPROD
'PROD' OPEN BHP 5* 95 /
/
TSTEP
2*10 /
END

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@ -1,276 +0,0 @@
-- This reservoir simulation is made available under the open Database
-- License: http://opendatacommons.org/licenses/odbl/1.0/
-- Individual contents of the database are licensed under the Database contents
-- License : http://opendatacommons.org/licenses/dbcl/1.0/
-- Copyright(C) 2015 Statoil
-- ===============================================================================
-- SPE 10 - MODEL 2
-- Simulation based on the followinf SPE paper:
-- "Tenth SPE comparative solution project: a comparison of upscaling techniques"
-- By Mike Christie (Heriot-Wat University) and Martin Blunt (Imperial College)
-- SPE, August 2001
-- ===============================================================================
RUNSPEC
TITLE
TENTH SPE COMPARATIVE SOLUTION PROJECT: A COMPARISON OF UPSCALING TECHNIQUES - MODEL 2
DIMENS
60 220 85 /
NONNC
OIL
WATER
GAS
FIELD
EQLDIMS
/
TABDIMS
/
WELLDIMS
5 340 1 5 /
UNIFOUT
START
1 'FEB' 1967 /
NSTACK
300 /
-- =================================================
------- In theis section, the geometry of the simulation
------- grid and the rock perøeabilities, porosities are
------- defined.
-- =================================================
GRID
INIT
OLDTRAN
INCLUDE
'SPE10MODEL2.GRDECL'
/
-- In the PORO file, all the values equal to 0 have been replaced
-- by a minimum by a minimum value (1e-7) in order not to have 'dead cells'.
INCLUDE
'SPE10MODEL2_PHI.INC'
/
INCLUDE
'SPE10MODEL2_PERM.INC'
/
MESSAGES
3* 100000 5* 100000 /
-- =======================================================
PROPS
--Sw Krw Kro
SWOF
0.200 0.0000 1.0000 0
0.250 0.0069 0.8403 0
0.300 0.0278 0.6944 0
0.350 0.0625 0.5625 0
0.400 0.1111 0.4444 0
0.450 0.1736 0.3403 0
0.500 0.2500 0.2500 0
0.550 0.3403 0.1736 0
0.600 0.4444 0.1111 0
0.650 0.5625 0.0625 0
0.700 0.6944 0.0278 0
0.750 0.8403 0.0069 0
0.800 1.0000 0.0000 0 /
-- No gas, but table needed because Flo is a 3-phase simulator
-- Sgmax is setto 0.8 to have coherent data with SWOF
-- simplest table has been considered
-- Sg Krg Kro Pcgo
SGOF
0.000000 0 1.000000 0.000000
0.800000 1 0.000000 0.000000 /
-- Oil Wat Gas
DENSITY
53 64 0.0624 /
PVDO
300 1.05 2.85
800 1.02 2.99
8000 1.01 3
/
PVTW
6000 1.01 0.000003 0.3 0 /
--PVT oif gas for 3-phi simulator flow - MADE UP DATA
PVDG
14.7 178.1 0.005
8000 1 0.01
/
ROCK
6000 0.000001
/
SOLUTION ========================================================
EQUIL
-- DATUM DATUM OWC OWC GOC GOC RSVD RVVD SOLN
-- DEPTH PRESS DEPTH PCOW DEPTH PCOG TABLE TABLE METH
12000 6000 12170 0 12000 0 1* 1* 0 /
SUMMARY ==========================================================
RUNSUM
FPR
FOPR
FOPT
FWPT
FWCT
WBHP
'INJ'
/
WOPR
'PRO1'
'PRO2'
'PRO3'
'PRO4'
/
WWCT
'PRO1'
'PRO2'
'PRO3'
'PRO4'
/
WOPT
'PRO1'
'PRO2'
'PRO3'
'PRO4'
/
SCHEDULE =====================================================
RPTRST
'BASIC=2' /
TUNING
/
/
2* 300 1* 12 /
WELSPECS
'INJ' 'G1' 30 110 12001 'WATER' /
'P1' 'G1' 1 1 12001 'OIL' /
'P2' 'G1' 60 1 12001 'OIL' /
'P3' 'G1' 60 220 12001 'OIL' /
'P4' 'G1' 1 220 12001 'OIL' /
/
COMPDAT
'INJ' 30 110 1 85 'OPEN' 2* 2 /
'P1' 1 1 1 85 'OPEN' 2* 2 /
'P2' 60 1 1 85 'OPEN' 2* 2 /
'P3' 60 220 1 85 'OPEN' 2* 2 /
'P4' 1 220 1 85 'OPEN' 2* 2 /
/
WCONINJE
'INJ' 'WATER' 'OPEN' 'RESV' 1* 5000 10000 /
/
WCONPROD
'P1' 'OPEN' 'BHP' 5* 4000 /
'P2' 'OPEN' 'BHP' 5* 4000 /
'P3' 'OPEN' 'BHP' 5* 4000 /
'P4' 'OPEN' 'BHP' 5* 4000 /
/
TSTEP
1 2 3 4 5 5 10 10 20 20 30 30 30 30 50 50 17*100 /
--DATES
-- $$$ 2 FEB 1967 /
-- $$$ 3 FEB 1967 /
-- $$$ 4 FEB 1967 /
-- $$$ 5 FEB 1967 /
-- $$$ 15 FEB 1967 /
-- $$$ 1 MAR 1967 /
-- $$$ 1 APR 1967 /
-- $$$ 1 MAY 1967 /
-- $$$ 1 AUG 1967 /
-- $$$ 1 NOV 1967 /
-- $$$ 1 FEB 1968 /
-- $$$ 1 MAY 1968 /
-- $$$ 1 AUG 1968 /
-- $$$ 1 NOV 1968 /
-- $$$ 1 FEB 1969 /
-- $$$ 1 MAY 1969 /
-- $$$ 1 AUG 1969 /
-- $$$ 1 NOV 1969 /
-- $$$ 1 FEB 1970 /
-- $$$ 1 MAY 1970 /
-- $$$ 1 AUG 1970 /
-- $$$ 1 NOV 1970 /
-- $$$ 1 FEB 1971 /
-- $$$ 1 MAY 1971 /
-- $$$ 1 AUG 1971 /
-- $$$ 1 NOV 1971 /
-- $$$ 1 FEB 1972 /
-- $$$ 1 MAY 1972 /
-- $$$ 24 JUL 1972 /
-- $$$ /
END

File diff suppressed because it is too large Load Diff