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run_0_6.out
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run_0_6.out
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********************************************************************************
* *
* STARS 2006.10 *
* Advanced Process and Thermal Reservoir Simulator *
* General Release for Win32 *
* 2006-May-24 16:32:32 *
* *
* (c) Copyright 1977 - 2006 *
* Computer Modelling Group Ltd., Calgary, Canada *
* All Rights Reserved *
* *
* *
* The license management portion of this application is based on: *
* SentinelLM* *
* (c) Copyright 1989-2006 SafeNet, Inc. *
* All rights reserved *
* *
********************************************************************************
Date and Time of Start of Run: Apr 13, 2012 02:57:03
RESULTS SIMULATOR STARS 200900
**NOLIST
**
INUNIT *SI
*****************************************************************
**CHECKONLY
**
INTERRUPT STOP
**
WPRN GRID TIME
WPRN ITER TIME
OUTPRN WELL ALL
**PRES SWCRIT SW SO SG TEMP OBHLOSS VISO KRO KRG KRW MASDENO MASDENG MASDENW
OUTPRN GRID NONE
**ALL **SMALL
OUTPRN RES NONE
OUTPRN ITER BRIEF
**
WSRF GRID TIME
WSRF WELL TIME
WSRF SECTOR TIME
OUTSRF GRID PRES SG SO SW TEMP
**OUTSRF WELL COMPONENT ALL
OUTSRF WELL LAYER ALL
REWIND 0
**$ Distance units: m
RESULTS XOFFSET 0.0000
RESULTS YOFFSET 0.0000
RESULTS ROTATION 0.0000 **$ (DEGREES)
RESULTS AXES-DIRECTIONS 1.0 -1.0 1.0
WRST TIME
**$ ***************************************************************************
**$ Definition of fundamental cartesian grid
**$ ***************************************************************************
GRID VARI 100 1 20
KDIR DOWN
DI IVAR
100*1
DJ JVAR
1
DK ALL
2000*1
DTOP
100*0
NULL CON 1
PINCHOUTARRAY CON 1
**$ Property: Porosity Max: 0.3 Min: 0.3
POR CON 0.32
**$ Property: Permeability I (md) Max: 4000 Min: 2000
PERMI CON 1000
*mod
INCLUDE 'K_Dyn/K_Dyn_0_6.inc'
1 1 20 = 2257.000
2 1 20 = 2056.500
3 1 20 = 1632.200
4 1 20 = 1511.900
5 1 20 = 1157.700
6 1 20 = 1408.200
7 1 20 = 569.660
8 1 20 = 637.140
9 1 20 = 699.260
10 1 20 = 559.910
11 1 20 = 1075.200
12 1 20 = 993.900
13 1 20 = 1624.200
14 1 20 = 1743.200
15 1 20 = 2658.000
16 1 20 = 2126.400
17 1 20 = 1664.700
18 1 20 = 2285.400
19 1 20 = 1696.700
20 1 20 = 1786.600
21 1 20 = 1200.700
.
.
.
PERMJ CON 1000
*mod
INCLUDE 'K_Dyn/K_Dyn_0_6.inc'
1 1 20 = 2257.000
2 1 20 = 2056.500
3 1 20 = 1632.200
4 1 20 = 1511.900
5 1 20 = 1157.700
6 1 20 = 1408.200
7 1 20 = 569.660
8 1 20 = 637.140
9 1 20 = 699.260
10 1 20 = 559.910
11 1 20 = 1075.200
12 1 20 = 993.900
13 1 20 = 1624.200
14 1 20 = 1743.200
15 1 20 = 2658.000
16 1 20 = 2126.400
17 1 20 = 1664.700
18 1 20 = 2285.400
19 1 20 = 1696.700
20 1 20 = 1786.600
21 1 20 = 1200.700
.
.
.
PERMK CON 1000
*mod
INCLUDE 'K_Dyn/K_Dyn_0_6.inc'
1 1 20 = 2257.000
2 1 20 = 2056.500
3 1 20 = 1632.200
4 1 20 = 1511.900
5 1 20 = 1157.700
6 1 20 = 1408.200
7 1 20 = 569.660
8 1 20 = 637.140
9 1 20 = 699.260
10 1 20 = 559.910
11 1 20 = 1075.200
12 1 20 = 993.900
13 1 20 = 1624.200
14 1 20 = 1743.200
15 1 20 = 2658.000
16 1 20 = 2126.400
17 1 20 = 1664.700
18 1 20 = 2285.400
19 1 20 = 1696.700
20 1 20 = 1786.600
21 1 20 = 1200.700
.
.
.
Loading Grid Module data into STARS arrays . . .
Done
END-GRID
*****************************************************************************
** GRID OTHER PROPERTIES
*****************************************************************************
ROCKTYPE 1
CPOR 1.2E-6
PRPOR 101.
CTPOR 3.84e-5
ROCKCP 2.347E6 0. ** J/(m3 C) = 35 Btu/(ft3 F)
***************************
THCONR 600E3 ** J/(m d C)
THCONW 55E3
THCONO 11E3
THCONG 2E3
THCONMIX SIMPLE
***************************
HLOSSPROP OVERBUR 2.347E6 1.496E5 ** Vol. Heat Capacity / Thermal conductivity
UNDERBUR 2.347E6 1.496E5
*********** Property: Thermal/rock Set Num Max: 1 Min: 1
THTYPE CON 1
*****************************************************************************
** COMPONENT PROPERTIES
*****************************************************************************
MODEL 3 3 3 1 **Fluids of the model include water, dead oil and methane
COMPNAME 'WATER' 'OIL' 'METHANE'
**--------------------------------
CMM 0.018 0.523 0.016 ** kg/gmol = kg/mol (!)
PCRIT 0.0 0.0 4600 ** kPa. Default for water, not needed for dead oil
TCRIT 0.0 0.0 -82.55 ** oC. Default for water, not needed for dead oil
MOLDEN 55555 1931 20000 ** Molar density = Dens/MW.
** For water =1000/0.018= 55555
** For oil = 1010/0.523 = 1931
** For gas = 320/0.016 = 20000
CP 4.463E-7 6E-7 10E-7 ** 1/kPa.
CT1 0.0 10.04E-4 9.72E-4 ** 1/oC. Thermal expansion coefficients
CT2 0.0 0.0 0.0
CPG1 0.0 841. 35.2 ** Refer to both ARC and CMG decks
CPL1 0.0 1000. 67.2
HVAPR 0.0 1346. 1770. ** Heat of vaporization, J/(gmol oC)
AVG 0.0 0.0 0.016
BVG 0.0 0.0 0.0 ** Temperature-independent
** K-VALUE CORRELATIONS (From STARS' Table)
KV1 0.0 0.0 5.45E5 **kPa.
KV4 0.0 0.0 -879.84 **oC
KV5 0.0 0.0 -265.99 **oC
PRSR 500. **kPa. Ref. pressure of methane & others density = Initial gas cap res. pressure
TEMR 10.
PSURF 101.3 **=14.7 psia **Surface conditions
TSURF 15.6 **=60 oF
VISCTABLE
************************************************** Both curves smoothed by Jeff
**Temp Water Bitumen Methane (liq)
**********************************************************************************
9.0 0 1461700 515.59
10.0 0 1241639 486.21
12.2 0 870699 427.72
40.0 0 22267.1 107.86
60.0 0 3183.8 49.21
80.0 0 694.3 25.58
100.0 0 209.2 14.74
120.0 0 81.1 9.23
140.0 0 38.2 6.17
160.0 0 21.1 4.37
175.6 0 14.5 3.44
200.0 0 9.1 2.48
220.0 0 6.8 1.97
240.0 0 5.4 1.6
260.0 0 4.5 1.34
280.0 0 4.0 1.13
300.0 0 3.6 0.98
350.0 0 3.2 0.80
*****************************************************************************
** ROCK-FLUID DATA
*****************************************************************************
ROCKFLUID
RPT 1
SWT
****************** Additional points were added between (1-Sor) and 1
** Sw Krw Krow
*************************************
0.15 0.0000 1.0000
0.20 0.0001 0.8603
0.25 0.0009 0.7305
0.30 0.0028 0.6106
0.35 0.0066 0.5009
0.40 0.0125 0.4014
0.45 0.0212 0.3123
0.50 0.0332 0.2337
0.55 0.0489 0.1659
0.60 0.0688 0.1091
0.65 0.0935 0.0635
0.70 0.1232 0.0296
0.75 0.1586 0.0080
0.80 0.2000 0.0000
0.85 0.2960 0.0000
0.90 0.4540 0.0000
0.95 0.6780 0.0000
1.00 1.0000 0.0000
SLT
******************* Additional points were added between Swc and (Swc+Sor)
**Sliq Krg Krog Krw
*************************************************
0.1500 1.0000 0.0000 0.0000
0.1925 0.8330 0.0000 0.0000
0.2775 0.6000 0.0000 0.0000
0.3625 0.4500 0.0000 0.0000
0.4050 0.3851 0.0081 0.0000
0.4475 0.3256 0.0277 0.0000
0.4900 0.2712 0.0570 0.0000
0.5325 0.2220 0.0951 0.0000
0.5750 0.1779 0.1415 0.0000
0.6175 0.1389 0.1957 0.0000
0.6600 0.1050 0.2575 0.0000
0.7025 0.0759 0.3266 0.0000
0.7450 0.0518 0.4028 0.0000
0.7875 0.0324 0.4859 0.0000
0.8300 0.0177 0.5758 0.0000
0.8725 0.0076 0.6722 0.0000
0.9150 0.0018 0.7751 0.0000
0.9575 0.0000 0.8844 0.0000
1.0000 0.0000 1.0000 0.0000
SGR 0.05 **Critical gas saturation
KRGCW 0.60 **Rel. perm. to gas at residual liquid saturation (Swc+Sor)
************* Sand
KRTEMTAB SORW SORG KRWIRO
10 0.15 0.15 0.20
250 0.10 0.05 0.40
************* RELATIVE PERMEABILITY TYPE DESIGNATION
************* Property: Rel Perm Set Number Max: 1 Min: 1
KRTYPE CON 1
************* Property: Critical Water Saturation Max: 0.15 Min: 0.15
BSWCRIT CON 0.15
*****************************************************************************
** INTITIALIZATION
*****************************************************************************
INITIAL
VERTICAL DEPTH_AVE
INITREGION 1
REFPRES 550
REFDEPTH 10
**$ Property: Temperature (C) Max: 10 Min: 10
TEMP CON 10
**$ Property: Water Saturation Max: 0.15 Min: 0.15
SW CON 0.2
**$ Property: Oil Saturation Max: 0.85 Min: 0.85
SO CON 0.8
**$ Property: Gas Saturation Max: 0 Min: 0
SG CON 0
** Initial "OIL" mol fraction in the oil liquid phase
**$ Property: Oil Mole Fraction(OIL) Max: 0.999 Min: 0.999
MFRAC_OIL 'OIL' CON 0.999
** Initial "METHANE" mol fraction in the oil liquid phase
**$ Property: Oil Mole Fraction(METHANE) Max: 0.001 Min: 0.001
MFRAC_OIL 'METHANE' CON 0.001
*****************************************************************************
** NUMERICAL CONTROL
*****************************************************************************
NUMERICAL
DTMAX 30.
MAXSTEPS 9999999
NORM TEMP 10
UPSTREAM KLEVEL
CONVERGE TOTRES LOOSE
ITERMAX 300
NORTH 100
*****************************************************************************
** WELL AND RECURRENT DATA
*****************************************************************************
NCUTS 20
===================== SUMMARY (from subroutine: INDATA) ======================
Reading of initial data is complete.
Simulation will stop if there were error messages.
0 Warning messages. 0 Error messages.
==============================================================================
1
=============================================
= =
= INPUT/OUTPUT CONTROL PARAMETERS =
= =
= Data Entered in the I/O Control Section =
= of Simulator Data =
= =
=============================================
Note: 1) All dimensioned quantities are in the user's input units.
2) Optional keywords may have been defaulted, i.e., were absent from the data.
3) All of the keywords in this section are optional.
4) A derived quantity has a blank in the Keyword column.
Description Value Keyword/Subkeyword
------------------------------------------------ -------------------- --------------------------------------------------
I/O Filenames: *FILENAMES
Input Data File run_0_6.dat
Main Output File run_0_6.out *OUTPUT 'run_0_6.out'
Output Index Results File (SR2 IRF) run_0_6.irf *INDEX-OUT 'run_0_6.irf'
Output Main Results File (SR2 MRF) run_0_6.mrf *MAIN-RESULTS-OUT 'run_0_6.mrf'
Project Identification Title #1 *TITLE1 ''
Project Identification Title #2 *TITLE2 ''
Run Identification Title *TITLE3 ''
Case Identification *CASEID ''
Material Basis Option Mole Basis Keyword *MASSBASIS was absent.
Basic Units of Input Data Modified SI Units *INUNIT *SI
Time day
Temperature Celsius
Pressure kPa
Length m
Property Vol m3
Permeability md
Mass kg
Molar Mass gmole
Viscosity cp
Energy J
Liquid Vol m3
Surf Tension Dyne/cm
Gas Volume m3
Basic Units of Output Quantities Modified SI Units *OUTUNIT *SI
Time day
Temperature Celsius
Pressure kPa
Length m
Property Vol m3
Permeability md
Mass kg
Molar Mass gmole
Viscosity cp
Energy J
Liquid Vol m3
Surf Tension Dyne/cm
Gas Volume m3
Frequency of Writing Restart Record Write at *TIME/*DATE *WRST *TIME
Frequency of Rewinding the Restart File Not Rewound *REWIND 0
Grid/Reservoir Definition Echo Off *OUTPRN *RES *NONE
Dispersed Component Particle Size 1.0E-17 m *PARTCLSIZE 1.0E-17
Well Quantities To Be Written (Output File) All Results *OUTPRN *WELL *ALL
Performance Statistics Info Freq. (Output File) Write at *TIME/*DATE *WPRN *ITER *TIME
Simulator Performance Statistics (Output File) Brief Summary *OUTPRN *ITER *BRIEF
Reservoir Condition Info Freq. (Output File) Write at *TIME/*DATE *WPRN *GRID *TIME
Reservoir Conditions To Be Written (Output File) Not Written *OUTPRN *GRID *NONE
Sector Statistics (Output File) Not Written *WPRN *SECTOR 0
Write Refined Grid Values (Output File) Yes *PRINT_REF *ON
Precision of Reals in Binary SR2 Files Double Precision *SR2PREC *DOUBLE
Format of Binary SR2 Files XDR Binary *XDR *ON
Well Performance Freq. (SR2 File) Write at *TIME/*DATE *WSRF *WELL *TIME
Well Performance Quantities (SR2 File) Surface Volumes for *OUTSRF *WELL
Each Well and Phase
+ No Components *COMPONENT *NONE
+ Layers *LAYER *ALL
+ No Moles (Subkeyword *MOLE absent)
+ No Mass (Subkeyword *MASS absent)
+ No Downhole Cond. (Subkeyword *DOWNHOLE absent)
Sector Statistics (SR2 File) Written *WSRF *SECTOR 1
Reservoir Condition Info Freq. (SR2 File) Write at *TIME/*DATE *WSRF *GRID *TIME
Reservoir Conditions To Be Written (SR2 File) *OUTSRF *GRID *PRES *SW *SO *SG *TEMP
Special Histories To Be Written (SR2 File) Not Written Keyword *OUTSRF *SPECIAL is absent
Maximum Timestep Number Allowed 9999999 *MAXSTEPS 9999999
Orientation of Grid Axes for Printout ( I, K, J) *PRNTORIEN 0 0
Data Checking Mode Option Do Timesteps Keyword *CHECKONLY is absent
Maximum Allowed Number of Errors 20 *MAXERROR 20
Matrix Solver Printout Off *OUTSOLVR *OFF
Action on Interrupt Trap Stop Immediately *INTERRUPT *STOP
1
****************************************************
* UNIT CONVERSIONS *
*--------------------------------------------------*
* MEASUREMENT INPUT UNIT OUTPUT UNIT *
* *
* Time day day *
* Temperature Celsius Celsius *
* Pressure kPa kPa *
* Length m m *
* Property Vol m3 m3 *
* Permeability md md *
* Mass kg kg *
* Molar Mass gmole gmole *
* Viscosity cp cp *
* Energy J J *
* Liquid Vol m3 m3 *
* Surf Tension Dyne/cm Dyne/cm *
* Gas Volume m3 m3 *
****************************************************
1
========================
= =
= FLUID DENSITY DATA =
= =
========================
Component Molecular Mole Mass Compress Thermal Critical Critical
Weight Density Density API -ibility Expansion Pressure Temperature
(kg/gmole ) (gmole /m3 ) (kg/m3 ) (1/kPa) (1/C) (kPa) (Cels)
WATER 1.8000E-02 5.5555E+04 1000. 9.9 4.463E-07 0.00 22048.00 374.20
OIL 0.5230 1931. 1010. 8.5 6.000E-07 1.004E-03 0.00 0.00
METHANE 1.6000E-02 2.0000E+04 320.0 310.3 1.000E-06 9.720E-04 4600.00 -82.55
Liquid Density Reference Conditions: Pressure = 500.00 kPa
Temperature = 10.00 Celsius
Density Mixing Rule
-------------------
Water Phase: Mixing rule is linear
Oil Phase: Mixing rule is linear
==============================
= =
= FLUID SURFACE CONDITIONS =
= =
==============================
Surface Pressure = 101.3 kPa
Surface Temperature = 15.60 Deg C
Surface Flash Option = Phases Segregated (K Values)
Ideal Gas Phase Density = 42.20 gmole/m3
Liquid Density Unit = gmole/m3
Surface Water Phase Oil Phase Gas-Liquid
Component Phase Density Density K Value
--------- ------- ----------- ---------- ----------
WATER w 5.5545E+04 3.7848E-03
OIL o 1920. 0.000
METHANE g 1.9884E+04 236.5
Liquid phase densities will be calculated when compositions are known.
1
***************************************************************************************************************
* SATURATED STEAM ENTHALPY TABLE *
* Temperature in Deg C, Pressure in kPa, Enthalpy in 1.0E+03 J/gmole *
*-------------------------------------------------------------------------------------------------------------*
* I I super- *
* temper pressr liquid vapour I temper pressr liquid vapour I temper critical *
* -ature enthalpy enthalpy I -ature enthalpy enthalpy I -ature enthalpy *
* I I *
* 0.00 0.02 -0.75676 44.27280 I 185.00 1164.53 13.38052 49.27447 I 374.15 39.24849 *
* 5.00 0.07 -0.37854 44.43991 I 190.00 1297.67 13.78102 49.34363 I 380.00 41.26966 *
* 10.00 0.17 0.00000 44.60675 I 195.00 1442.33 14.18342 49.41086 I 390.00 44.72466 *
* 15.00 0.35 0.37764 44.77320 I 200.00 1599.18 14.58792 49.46869 I 400.00 48.17966 *
* 20.00 0.66 0.75510 44.93910 I 205.00 1768.93 14.99452 49.51905 I 410.00 49.36717 *
* 25.00 1.16 1.13184 45.10430 I 210.00 1952.33 15.40352 49.56277 I 420.00 50.55468 *
* 30.00 1.89 1.50804 45.26862 I 215.00 2150.13 15.81502 49.59410 I 430.00 51.61774 *
* 35.00 2.94 1.88406 45.43192 I 220.00 2363.12 16.22902 49.62440 I 440.00 52.55636 *
* 40.00 4.39 2.26008 45.59405 I 225.00 2592.11 16.64582 49.65568 I 450.00 53.49497 *
* 45.00 6.35 2.63592 45.75490 I 230.00 2837.93 17.06602 49.66573 I 460.00 54.18820 *
* 50.00 8.93 3.01176 45.91453 I 235.00 3101.45 17.48902 49.67031 I 470.00 54.88142 *
* 55.00 12.25 3.38796 46.07353 I 240.00 3383.54 17.91562 49.66517 I 480.00 55.57465 *
* 60.00 16.46 3.76416 46.23048 I 245.00 3685.13 18.34592 49.66248 I 490.00 56.26787 *
* 65.00 21.72 4.14090 46.38523 I 250.00 4007.14 18.78032 49.63664 I 500.00 56.96110 *
* 70.00 28.18 4.51746 46.53770 I 255.00 4350.54 19.21892 49.59876 I 510.00 57.54712 *
* 75.00 36.05 4.89456 46.68784 I 260.00 4716.32 19.66252 49.55291 I 520.00 58.13313 *
* 80.00 45.52 5.27220 46.83568 I 265.00 5105.49 20.11082 49.50436 I 530.00 58.71915 *
* 85.00 56.82 5.65002 46.98657 I 270.00 5519.10 20.56502 49.43957 I 540.00 59.30516 *
* 90.00 70.18 6.02838 47.13515 I 275.00 5958.22 21.02512 49.35660 I 550.00 59.89118 *
* 95.00 85.85 6.40710 47.27550 I 280.00 6423.95 21.49162 49.24283 I 560.00 60.42755 *
* 100.00 104.10 6.78654 47.40679 I 285.00 6917.40 21.96542 49.14859 I 570.00 60.96391 *
* 105.00 125.23 7.16652 47.54450 I 290.00 7439.73 22.44712 49.00622 I 580.00 61.50028 *
* 110.00 149.54 7.54722 47.67912 I 295.00 7992.13 22.93722 48.89003 I 590.00 62.03665 *
* 115.00 177.35 7.92846 47.81072 I 300.00 8575.79 23.43582 48.74339 I 600.00 62.57301 *
* 120.00 209.02 8.31060 47.93902 I 305.00 9191.96 23.94702 48.53745 I 610.00 63.08122 *
* 125.00 244.90 8.69364 48.06346 I 310.00 9841.89 24.46722 48.33974 I 620.00 63.58943 *
* 130.00 285.39 9.07740 48.18550 I 315.00 10526.89 25.00182 48.09716 I 630.00 64.09764 *
* 135.00 330.87 9.46222 48.30537 I 320.00 11248.26 25.55082 47.82999 I 640.00 64.60585 *
* 140.00 381.78 9.84812 48.42178 I 325.00 12007.38 26.12502 47.56418 I 650.00 65.11406 *
* 145.00 438.57 10.23512 48.53697 I 330.00 12805.60 26.69922 47.17849 I 660.00 65.60501 *
* 150.00 501.69 10.62342 48.64384 I 335.00 13644.35 27.31932 46.69945 I 670.00 66.09596 *
* 155.00 571.63 11.01292 48.74784 I 340.00 14525.06 27.93942 46.39002 I 680.00 66.58691 *
* 160.00 648.90 11.40372 48.84684 I 345.00 15449.20 28.62702 46.13799 I 690.00 67.07786 *
* 165.00 734.04 11.79592 48.94188 I 350.00 16418.27 29.31462 45.63539 I 700.00 67.56881 *
* 170.00 827.58 12.18962 49.03314 I 355.00 17433.79 30.12372 44.88992 I 710.00 68.04477 *
* 175.00 930.11 12.58492 49.11873 I 360.00 18497.34 30.93282 43.87824 I 720.00 68.52073 *
* 180.00 1042.22 12.98182 49.19963 I 365.00 19610.48 32.10282 43.04307 I 730.00 68.99668 *
* 185.00 1164.53 13.38052 49.27447 I 370.00 20774.86 33.27282 41.40433 I 740.00 69.47264 *
* *
***************************************************************************************************************
Table based on zero liquid enthalpy at 10.00 Deg C
1 =======================================================
= =
= RELATIVE PERMEABILITY AND CAPILLARY PRESSURE DATA =
= =
=======================================================
T (C) Swcon Soirw Sgcon Soirg Swcrit Sorw Sgr Sorg Krwiro Krocw Krgcw
------ ------ ------ ------ ------ ------ ------ ------ ------ ------ ------ ------
10.0 0.1500 0.0000 0.0000 0.0000 0.1500 0.1500 0.0500 0.1500 0.2000 1.0000 0.6000
250.0 0.1500 0.0000 0.0000 0.0000 0.1500 0.1000 0.0500 0.0500 0.4000 1.0000 0.6000
*** DATA AT TEMPERATURE OF 10.00 C ***
--- WATER-OIL SYSTEM ---
Sw1 Krw Sw2 Krow Sw3 Pcow
--- --- --- ---- --- ----
0.1500 0.0000 0.1500 1.0000 0.1500 0.0000
0.2000 0.0000 0.2038 0.8603 0.2000 0.0000
0.2500 0.0002 0.2577 0.7305 0.2500 0.0000
0.3000 0.0006 0.3115 0.6106 0.3000 0.0000
0.3500 0.0013 0.3654 0.5009 0.3500 0.0000
0.4000 0.0025 0.4192 0.4014 0.4000 0.0000
0.4500 0.0042 0.4731 0.3123 0.4500 0.0000
0.5000 0.0066 0.5269 0.2337 0.5000 0.0000
0.5500 0.0098 0.5808 0.1659 0.5500 0.0000
0.6000 0.0138 0.6346 0.1091 0.6000 0.0000
0.6500 0.0187 0.6885 0.0635 0.6500 0.0000
0.7000 0.0246 0.7423 0.0296 0.7000 0.0000
0.7500 0.0317 0.7962 0.0080 0.7500 0.0000
0.8000 0.0400 0.8500 0.0000 0.8000 0.0000
0.8500 0.0592 0.9038 0.0000 0.8500 0.0000
0.9000 0.0908 0.9577 0.0000 0.9000 0.0000
0.9500 0.1356 1.0115 0.0000 0.9500 0.0000
1.0000 0.2000 1.0654 0.0000 1.0000 0.0000
--- LIQUID(OIL)-GAS SYSTEM ---
Sw So Sl1 Krg Sl2 Krog Sl3 Pcgo
-- -- --- --- --- ---- --- ----
0.1500 0.0000 0.1500 0.6000 0.0667 0.0000 0.1500 0.0000
0.1500 0.0421 0.1921 0.4998 0.1133 0.0000 0.1925 0.0000
0.1500 0.1263 0.2763 0.3600 0.2067 0.0000 0.2775 0.0000
0.1500 0.2105 0.3605 0.2700 0.3000 0.0000 0.3625 0.0000
0.1500 0.2526 0.4026 0.2311 0.3467 0.0081 0.4050 0.0000
0.1500 0.2947 0.4447 0.1954 0.3933 0.0277 0.4475 0.0000
0.1500 0.3368 0.4868 0.1627 0.4400 0.0570 0.4900 0.0000
0.1500 0.3789 0.5289 0.1332 0.4867 0.0951 0.5325 0.0000
0.1500 0.4211 0.5711 0.1067 0.5333 0.1415 0.5750 0.0000
0.1500 0.4632 0.6132 0.0833 0.5800 0.1957 0.6175 0.0000
0.1500 0.5053 0.6553 0.0630 0.6267 0.2575 0.6600 0.0000
0.1500 0.5474 0.6974 0.0455 0.6733 0.3266 0.7025 0.0000
0.1500 0.5895 0.7395 0.0311 0.7200 0.4028 0.7450 0.0000
0.1500 0.6316 0.7816 0.0194 0.7667 0.4859 0.7875 0.0000
0.1500 0.6737 0.8237 0.0106 0.8133 0.5758 0.8300 0.0000
0.1500 0.7158 0.8658 0.0046 0.8600 0.6722 0.8725 0.0000
0.1500 0.7579 0.9079 0.0011 0.9067 0.7751 0.9150 0.0000
0.1500 0.8000 0.9500 0.0000 0.9533 0.8844 0.9575 0.0000
0.1500 0.8421 0.9921 0.0000 1.0000 1.0000 1.0000 0.0000
Liquid saturation includes critical wetting phase
THREE-PHASE WATER-OIL-GAS SUMMARY
=================================
Middle Phase Relative Permeability Calculated From Stone's Model II
Wettability: Water phase is wetting phase; oil phase is middle phase
so= 0 so= 10 so= 20 so= 30 so= 40 so= 50 so= 60 so= 70 so= 80 so= 90 so=100
-------------------------------------------------------------------------------------------------------------------------
sw= 0 krw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
kro 0.00000 0.00000 0.00000 0.00000 0.03189 0.10836 0.22219 0.37014 0.55011 0.76040 1.00000
krg 0.60000 0.60000 0.48669 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 10 krw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
kro 0.00000 0.00000 0.00000 0.03189 0.10836 0.22219 0.37014 0.55011 0.76040 1.00000
krg 0.60000 0.48669 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 20 krw 0.00002 0.00002 0.00002 0.00002 0.00002 0.00002 0.00002 0.00002 0.00002
kro 0.00000 0.00000 0.00000 0.07437 0.18159 0.31633 0.47672 0.66153 0.87028
krg 0.48669 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 30 krw 0.00056 0.00056 0.00056 0.00056 0.00056 0.00056 0.00056 0.00056
kro 0.00000 0.00000 0.01271 0.10802 0.21896 0.34412 0.48307 0.63629
krg 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 40 krw 0.00250 0.00250 0.00250 0.00250 0.00250 0.00250 0.00250
kro 0.00000 0.00000 0.04432 0.13513 0.23051 0.33068 0.43694
krg 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0--------
sw= 50 krw 0.00664 0.00664 0.00664 0.00664 0.00664 0.00664
kro 0.00000 0.00000 0.06471 0.13597 0.20475 0.27300
krg 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0--------
sw= 60 krw 0.01376 0.01376 0.01376 0.01376 0.01376
kro 0.00000 0.00771 0.06082 0.10597 0.14561
krg 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0--------
sw= 70 krw 0.02464 0.02464 0.02464 0.02464
kro 0.00000 0.00553 0.03527 0.05624
krg 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0--------
sw= 80 krw 0.04000 0.04000 0.04000
kro 0.00000 0.00000 0.00743
krg 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000
------------0---------0---------0--------
sw= 90 krw 0.09080 0.09080
kro 0.00000 0.00000
krg 0.00173 0.00000
prscw 0.00000 0.00000
prscg 0.00000 0.00000
------------0---------0--------
sw=100 krw 0.20000
kro 0.00000
krg 0.00000
prscw 0.00000
prscg 0.00000
------------0--------
1
*** DATA AT TEMPERATURE OF 250.00 C ***
--- WATER-OIL SYSTEM ---
Sw1 Krw Sw2 Krow Sw3 Pcow
--- --- --- ---- --- ----
0.1500 0.0000 0.1500 1.0000 0.1500 0.0000
0.2000 0.0000 0.2077 0.8603 0.2000 0.0000
0.2500 0.0004 0.2654 0.7305 0.2500 0.0000
0.3000 0.0011 0.3231 0.6106 0.3000 0.0000
0.3500 0.0026 0.3808 0.5009 0.3500 0.0000
0.4000 0.0050 0.4385 0.4014 0.4000 0.0000
0.4500 0.0085 0.4962 0.3123 0.4500 0.0000
0.5000 0.0133 0.5538 0.2337 0.5000 0.0000
0.5500 0.0196 0.6115 0.1659 0.5500 0.0000
0.6000 0.0275 0.6692 0.1091 0.6000 0.0000
0.6500 0.0374 0.7269 0.0635 0.6500 0.0000
0.7000 0.0493 0.7846 0.0296 0.7000 0.0000
0.7500 0.0634 0.8423 0.0080 0.7500 0.0000
0.8000 0.0800 0.9000 0.0000 0.8000 0.0000
0.8500 0.1184 0.9577 0.0000 0.8500 0.0000
0.9000 0.1816 1.0154 0.0000 0.9000 0.0000
0.9500 0.2712 1.0731 0.0000 0.9500 0.0000
1.0000 0.4000 1.1308 0.0000 1.0000 0.0000
--- LIQUID(OIL)-GAS SYSTEM ---
Sw So Sl1 Krg Sl2 Krog Sl3 Pcgo
-- -- --- --- --- ---- --- ----
0.1500 0.0000 0.1500 0.6000 -0.0667 0.0000 0.1500 0.0000
0.1500 0.0421 0.1921 0.4998 -0.0133 0.0000 0.1925 0.0000
0.1500 0.1263 0.2763 0.3600 0.0933 0.0000 0.2775 0.0000
0.1500 0.2105 0.3605 0.2700 0.2000 0.0000 0.3625 0.0000
0.1500 0.2526 0.4026 0.2311 0.2533 0.0081 0.4050 0.0000
0.1500 0.2947 0.4447 0.1954 0.3067 0.0277 0.4475 0.0000
0.1500 0.3368 0.4868 0.1627 0.3600 0.0570 0.4900 0.0000
0.1500 0.3789 0.5289 0.1332 0.4133 0.0951 0.5325 0.0000
0.1500 0.4211 0.5711 0.1067 0.4667 0.1415 0.5750 0.0000
0.1500 0.4632 0.6132 0.0833 0.5200 0.1957 0.6175 0.0000
0.1500 0.5053 0.6553 0.0630 0.5733 0.2575 0.6600 0.0000
0.1500 0.5474 0.6974 0.0455 0.6267 0.3266 0.7025 0.0000
0.1500 0.5895 0.7395 0.0311 0.6800 0.4028 0.7450 0.0000
0.1500 0.6316 0.7816 0.0194 0.7333 0.4859 0.7875 0.0000
0.1500 0.6737 0.8237 0.0106 0.7867 0.5758 0.8300 0.0000
0.1500 0.7158 0.8658 0.0046 0.8400 0.6722 0.8725 0.0000
0.1500 0.7579 0.9079 0.0011 0.8933 0.7751 0.9150 0.0000
0.1500 0.8000 0.9500 0.0000 0.9467 0.8844 0.9575 0.0000
0.1500 0.8421 0.9921 0.0000 1.0000 1.0000 1.0000 0.0000
Liquid saturation includes critical wetting phase
THREE-PHASE WATER-OIL-GAS SUMMARY
=================================
Middle Phase Relative Permeability Calculated From Stone's Model II
Wettability: Water phase is wetting phase; oil phase is middle phase
so= 0 so= 10 so= 20 so= 30 so= 40 so= 50 so= 60 so= 70 so= 80 so= 90 so=100
-------------------------------------------------------------------------------------------------------------------------
sw= 0 krw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
kro 0.00000 0.00000 0.00000 0.02525 0.08557 0.17537 0.29205 0.43396 0.59990 0.78876 1.00000
krg 0.60000 0.60000 0.48669 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 10 krw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
kro 0.00000 0.00000 0.02525 0.08557 0.17537 0.29205 0.43396 0.59990 0.78876 1.00000
krg 0.60000 0.48669 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 20 krw 0.00004 0.00004 0.00004 0.00004 0.00004 0.00004 0.00004 0.00004 0.00004
kro 0.00000 0.00000 0.04692 0.13553 0.24569 0.37600 0.52537 0.69305 0.87893
krg 0.48669 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 30 krw 0.00112 0.00112 0.00112 0.00112 0.00112 0.00112 0.00112 0.00112
kro 0.00000 0.00000 0.06233 0.16069 0.26997 0.38932 0.51862 0.65856
krg 0.33469 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0---------0--------
sw= 40 krw 0.00500 0.00500 0.00500 0.00500 0.00500 0.00500 0.00500
kro 0.00000 0.00000 0.08526 0.17661 0.27038 0.36696 0.46773
krg 0.23349 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0---------0--------
sw= 50 krw 0.01328 0.01328 0.01328 0.01328 0.01328 0.01328
kro 0.00000 0.01866 0.09540 0.16830 0.23821 0.30706
krg 0.15349 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0---------0--------
sw= 60 krw 0.02752 0.02752 0.02752 0.02752 0.02752
kro 0.00000 0.02690 0.08429 0.13436 0.17946
krg 0.09065 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0---------0--------
sw= 70 krw 0.04928 0.04928 0.04928 0.04928
kro 0.00000 0.01765 0.05496 0.08478
krg 0.04464 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000 0.00000
------------0---------0---------0---------0--------
sw= 80 krw 0.08000 0.08000 0.08000
kro 0.00000 0.00035 0.02384
krg 0.01558 0.00173 0.00000
prscw 0.00000 0.00000 0.00000
prscg 0.00000 0.00000 0.00000
------------0---------0---------0--------
sw= 90 krw 0.18160 0.18160
kro 0.00000 0.00000
krg 0.00173 0.00000
prscw 0.00000 0.00000
prscg 0.00000 0.00000
------------0---------0--------
sw=100 krw 0.40000
kro 0.00000
krg 0.00000
prscw 0.00000
prscg 0.00000
------------0--------
Hysteresis Data for Current Rock-Fluid Set
------------------------------------------
Oil Relative Permeability Disabled
Water Relative Permeability Disabled
Gas Relative Permeability Disabled
Oil-Water Capillary Pressure Disabled
Oil-Gas Capillary Pressure Disabled
1 ========================================
= =
= EQUILIBRIUM VAPOUR/LIQUID K VALUES =
= =
========================================
--- WATER y/w ---
pressure (kPa)
T (C) 200 400 600 800 2000 4000 6000 8000 20000 40000 60000 80000
----- -----------------------------------------------------------------------------------------------------------------------
25 5.775E-03 2.888E-03 1.925E-03 1.444E-03 5.775E-04 2.888E-04 1.925E-04 1.444E-04 5.775E-05 2.888E-05 1.925E-05 1.444E-05
50 4.465E-02 2.233E-02 1.488E-02 1.116E-02 4.465E-03 2.233E-03 1.488E-03 1.116E-03 4.465E-04 2.233E-04 1.488E-04 1.116E-04
100 0.521 0.260 0.174 0.130 5.205E-02 2.603E-02 1.735E-02 1.301E-02 5.205E-03 2.603E-03 1.735E-03 1.301E-03
150 2.51 1.25 0.836 0.627 0.251 0.125 8.362E-02 6.271E-02 2.508E-02 1.254E-02 8.362E-03 6.271E-03
200 8.00 4.00 2.67 2.00 0.800 0.400 0.267 0.200 7.996E-02 3.998E-02 2.665E-02 1.999E-02
250 20.0 10.0 6.68 5.01 2.00 1.00 0.668 0.501 0.200 0.100 6.679E-02 5.009E-02
300 42.9 21.4 14.3 10.7 4.29 2.14 1.43 1.07 0.429 0.214 0.143 0.107
400 145. 72.3 48.2 36.2 14.5 7.23 4.82 3.62 1.45 0.723 0.482 0.362
600 823. 411. 274. 206. 82.3 41.1 27.4 20.6 8.23 4.11 2.74 2.06
800 2.862E+03 1.431E+03 954. 716. 286. 143. 95.4 71.6 28.6 14.3 9.54 7.16
1000 7.569E+03 3.785E+03 2.523E+03 1.892E+03 757. 378. 252. 189. 75.7 37.8 25.2 18.9
--- OIL y/x ---
pressure (kPa)
T (C) 200 400 600 800 2000 4000 6000 8000 20000 40000 60000 80000
----- -----------------------------------------------------------------------------------------------------------------------
25 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
50 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
100 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
150 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
200 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
250 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
300 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
400 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
600 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
800 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
1000 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
--- METHANE y/x ---
pressure (kPa)
T (C) 200 400 600 800 2000 4000 6000 8000 20000 40000 60000 80000
----- -----------------------------------------------------------------------------------------------------------------------
25 133. 66.3 44.2 33.1 13.3 6.63 4.42 3.31 1.33 0.663 0.442 0.331
50 168. 84.2 56.1 42.1 16.8 8.42 5.61 4.21 1.68 0.842 0.561 0.421
100 246. 123. 82.1 61.6 24.6 12.3 8.21 6.16 2.46 1.23 0.821 0.616
150 329. 164. 110. 82.2 32.9 16.4 11.0 8.22 3.29 1.64 1.10 0.822
200 412. 206. 137. 103. 41.2 20.6 13.7 10.3 4.12 2.06 1.37 1.03
250 495. 248. 165. 124. 49.5 24.8 16.5 12.4 4.95 2.48 1.65 1.24
300 576. 288. 192. 144. 57.6 28.8 19.2 14.4 5.76 2.88 1.92 1.44
400 727. 364. 242. 182. 72.7 36.4 24.2 18.2 7.27 3.64 2.42 1.82
600 987. 493. 329. 247. 98.7 49.3 32.9 24.7 9.87 4.93 3.29 2.47
800 1.194E+03 597. 398. 298. 119. 59.7 39.8 29.8 11.9 5.97 3.98 2.98
1000 1.360E+03 680. 453. 340. 136. 68.0 45.3 34.0 13.6 6.80 4.53 3.40