texaco e&p inc. t - pe.tamu.edu · api gravity = gar @ std 19.88 0.772 g/cm3 at 28.2 0 api 241...
TRANSCRIPT
from Texaco E&P Inc.'s MC 291. aCS-G-8805. Well #1. This fluid was a !2lackoil as characterized bv its GaR (- 950 scf/STB) and measured phase behavior.
Reservoir Conditions:Pressure: 6017 psiaTemperature: 157°F
Sample Information:3 MDT bottomhole samples in MPSRs from the 11.456' interval.Additional MDT samples for other zones analvzed in other reports.
Fluid Properties of Oil from MPSR 380:GaR: 967 scf/STBS~turated FVF: 1.433 vol @ psat.Tres / vol @ std
API gravitv: 28.1°APISaturation Pressure: 5150 psia (@ 157°F)Reservoir Fluid Viscositv: 1.14 cp (@ 6017 psia. 157°F)
1.0 INTRODUCTION
Texaco Exploration and Production Inc., of New Orleans, La., was interested inobtaining fluid volumetric and compositional data for a selected bottomhole reservoir oilfrom Well #1, Mississippi Canyon block 291, 11,456 ft interval (note, three samples
MC291, Well #1: 11,456 Interval -Black Oil Study, 1DBRFPI -407109A
TEXACO -MISSISSIPPI CANYON 291, Well #1:11,456 ft INTERVAL
BLACK OIL PVT STUDY ~c/ I. '-'S
~\' L1\ -q1Qq ~\TEXACO E&P INC. t
MISSISSIPPI CANYON 291. WELL #111.456' INTERVALBLACK OIL STUDY
TABLE 3.1
TEXACO -MISSISSIPPI CANYON 291, Well #1:11,456 ft INTERVAL
C24+ COMPOSITION OF MPSR 213
GASMOLE %
GROUPMOLE %
LIQUIDWT%
OVERALLWT % MOLE %COMPONENT MW
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00450.00
0.0850.0000.281
86.5833.7303.5390.7572.1220.7600.9050.7080.1040.0150.0440.1950.0500.0080.0700.0070.0120.0020.0150.0060.0010.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.0000.0000.0000.0100.0090.0560.0390.1800.2300.3911.7620.3720.0520.2321.6390.7660.1932.2680.3560.5810.2181.9213.2432.9622.8362.8372.9032.9265.7204.2474.5273.5502.9972.2152.0111.293
44.457
0.0240.0000.0508.8710.7231.0450.3150.9430.5500.7561.9190.3790.0530.2241.5470.6960.1732.0200.3140.5120.1901.6802.8192.5722.4612.4632.5202.5404.9653.6873.9293.0812.6011.9231.7451.123
38.588
0.0540.0000.178
54.8822.3882.3520.5381.6110.7561.0402.2100.4470.0670.2711.5320.7030.1861.7550.2940.4790.1781.3002.0881.7371.5171.3971.3161.2242.2201.5441.5541.1630.9390.6560.5680.3508.511
0.0540.0000.178
54.8822.3882.3520.5381.6110.7561.040
2.994
CO2H2SN2C1C2C3I-C4N-C4I-CSN-CSC6MCYC-CSBENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEa-XYLENEC9C10C11C12C13C14C1SC16C17C18C19C20C21C22C23C24+
6.427
8.055
7.704
2.5138.511
20.690.756 g/cm3 at
29.3 0 API
234.87MW (Ib/lbmole)DENSITY=API GRAVITY =
GaR @ STD
99.258000 psia160 of. &
843 (SCF/BBL)150 (M3/M3)
MC291, Well #1: 11,456 Interval -Black Oil Study, 10DBRFPI-407109A
TABLE 3.2
TEXACO -MISSISSIPPI CANYON 291, Well #1 :11,456 ft INTERVAL
C24+ COMPOSITION OF MPSR 301
GASMOLE %
LIQUIDWT%
OVERALLWT % MOLE %
GROUPMOLE %COMPONENT MW
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEO-XYLENEC9C10C11C12C13C14C15C16C17C18C19C20C21C22C23C24+
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00450.00
0.0870.0000.285
88.0143.7923.4080.6451.7720.5510.6270.4560.0830.0100.0370.1180.0490.0070.0410.0020.0070.0010.0050.0040.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.0000.0000.0000.0000.0000.0640.0000.3020.2930.4821.2890.3950.0540.2411.7030.7810.1952.2940.3570.5780.2151.9283.2342.9512.8292.8882.9052.9903.0303.6033.3802.7172.8092.5232.2341.503
49.233
0.0270.0000.0569.8790.7981.1070.2620.9800.5300.7311.3850.3890.0520.2291.5490.7050.1722.0080.3090.5030.1861.6652.7872.5402.4352.4862.5012.5742.6083.1022.9102.3392.4192.1721.9241.294
42.386
0.0570.0000.189
58.2752.5112.3750.4271.5960.6960.9591.5200.4370.0630.2641.4630.6800.1771.6630.2760.4480.1661.2281.9681.6351.4311.3451.2461.1831.1121.2381.0970.8420.8320.7060.5970.3858.914
0.0570.0000.189
58.2752.5112.3750.4271.5960.6960.959
2.284
6.100
7.625
5.472
2.5218.914
MW (Ib/lbmole)DENSITY=API GRAVITY =
GaR @ STD
19.88
0.772 g/cm3 at28.2 0 API
241 .12 94.638000 psi a75 of. &
169 (M3/M3) 946 (SCF/BBL)
MC291, Well #1: 11,456 Interval -Black Oil Study, 11DBRFPI-407109A
TABLE 3.3
TEXACO -MISSISSIPPI CANYON 291, Well #1:11,456 ft INTERVAL
C24+ COMPOSITION OF MPSR 380
GASMOLE %
LIQUIDWT%
OVERALLWT % MOLE %
GROUPMOLE %COMPONENT MW
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEa-XYLENEC9C10C11C12C13C14C15C16C17C18C19C20C21C22C23C24+
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00450.00
0.0910.0000.294
88.6833.4583.1360.6121.7360.5720.6620.4050.0890.0100.0380.1190.0470.0060.0360.0020.0020.0000.0020.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.0000.0000.0000.0010.0030.0310.0300.1460.2170.3761.1260.3670.0510.2291.6480.7610.1912.2630.3540.5760.2111.9223.2282.9452.8102.7992.8702.9513.6002.7283.1772.9832.6532.6352.4961.802
49.820
0.0290.0000.059
10.2420.7511.0220.2810.8520.4830.6661.2170.3690.0500.2201.5000.6860.1691.9710.3050.4960.1821.6512.7702.5272.4122.4022.4632.5323.0892.3412.7262.5602.2772.2612.1421.546
42.751
0.0610.0000.198
59.7272.3362.1690.4531.3710.6260.8641.3210.4100.0590.2501.4010.6540.1711.6150.2690.4370.1601.2041.9341.6081.4011.2841.2131.1501.3020.9241.0160.9100.7750.7270.6570.4558.888
0.0610.0000.198
59.7272.3362.1690.4531.3710.6260.864
2.040
5.910
7.440
5.302
2.6138.888
MW (Ib/lbmole)DENSITY=API GRAVITY =
GaR @ STD
19.710.772 g/cm3 at28.1 °API
245.84 93.558000 psia75 of. &
172 (M3/M3) 967 (SCF/BBL)
MC291, Well #1: 11 ,456 Interval- Black Oil Study, 12DBRFPI -407109A
TABLE 3.4TEXACO -MISSISSIPPI CANYON 291, Well #1:
MPSR 380: 11,456 ft INTERVAL, C30+ COMPOSITION
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEa-XYLENEC9C10C11C12C13C14C15C16C17C18C19C20C21C22C23C24C25C26C27C28C29C30+
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00331.00345.00359.00374.00388.00402.00580.00
0.0910.0000.294
88.6833.4583.1360.6121.7360.5720.6620.4050.0890.0100.0380.1190.0470.0060.0360.0020.0020.0000.0020.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.0000.0000.0000.0000.0000.0620.0520.2480.3010.4951.3480.3690.0480.2911.8160.7400.2012.5520.1220.4460.1802.4553.5143.1322.9263.2222.9683.0643.6492.5853.1892.5152.3552.1672.0751.8171.8171.6321.5151.4341.3491.489
39.859
0.0290.0000.059
10.2420.7491.0490.3010.9390.5550.7681.4080.3710.0470.2721.6440.6680.1762.2200.1060.3850.1552.1083.0152.6882.5112.7642.5472.6293.1322.2182.7372.1582.0211.8601.7801.5591.5601.4011.3001.2311.1581.277
34.204
0.0610.0000.198
59.8052.3322.2280.4841.5140.7210.9981.5300.4130.0560.3111.5370.6370.1791.8200.0940.3400.1371.5392.1081.7131.4611.4801.2561.1961.3210.8771.0210.7690.6880.5990.5470.4590.4410.3800.3390.3080.2800.2985.525
0.0610.0000.198
59.8052.3322.2280.4841.5140.7210.998
2.309
6.283
8.018
5.184
4.3405.525
MW (Ib/lbmole) =DENSITY =GOR @ STD
19.71 246.870.772 g/cm;j @ 75°F & 8000 psi a
172 (M3/M3)
93.68
967 (SCF/STB)
MC291, Well #1: 11,456 Interval- Black Oil Study, 13DBRFPI- 407109A
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TABLE 4.2
TEXACO -MISSISSIPPI CANYON 291, Well #1 :
MPSR 380, 11,456 ft INTERVAL:GOR DATA -DIFFERENTIAL LIBERATION @ 157°F
Pressure(psia)
CumulativeProduced
GOR1
SolutionGas GOR1
Rs
5150
3500
2000
1000
300
85
15.025
B.P. 0
418
663
801
906
932
958
958
540
295
157
52
26
0
1. Standard Cubic Feet of Gas I bbl of Oil @ 15.025 psia and 60°F
DBRFPI- 407109A MC291, Well #1: 11,456 Inte/Val- Black Oil Study, 17
TABLE 4.3
TEXACO -MISSISSIPPI CANYON 291, Well #1 :
MPSR 380, 11,456 ft INTERVAL:VAPOR PHASE DATA -DIFFERENTIAL LIBERATION @ 157°F
Pressure
(psia)Vapor
Density(g/cc)
VaporMolecular
Mass (g/mol)
VaporGravity1
VaporViscosity
(cP)
ZFactor
5150
3500
2000
1000
300
85
15.025
B.P.
0.181
0.106
0.047
0.015
0.004
0.001
17.86
17.78
17.93
19.75
25.75
40.07
0.616
0.614
0.619
0.682
0.889
1.383
0.882
0.868
0.909
0.964
0.985
0.994
0.022
0.016
0.014
0.012
0.011
0.010
1. Vapor Phase MW / MW of Air2. z = PV/nRT
DBRFPI- 407109A MC291, Well #1: 11,456 Interval -Black Oil Study, 19
TABLE 4.4
TEXACO -MISSISSIPPI CANYON 291, Well #1 :
MPSR 380, 11,456 ft INTERVAL:LIQUID PHASE DATA -DIFFERENTIAL LIBERATION @ 157°F
Pressure
(psia)
Oil Density(g/cm3)
Oil FVF
80(1)
Oil Viscosity(cP)
1.402
1.419
1.267
1.165
1.110
1.070
1.061
1.039
6017
5150
3500
2000
1000
300
85
15.025
0.733
0.724(2)
0.766
0.804
0.826
0.843
0.845
0.846
1.14
1.15
2.20
2.67
3.10
3.73
4.10
4.32
1. bbl of Reservoir Oil @ P, T per bbl of Oil at 15.025 psia and GO°F2. Density from CCE Test
MC291, Well #1: 11 ,456 Interval- Black Oil Study, 21DBRFPI-407109A
FIGURE 4.4
TEXACO -MISSISSIPPI CANYON 291, Well #1 :
MPSR 380, 11,456 ft INTERVALLIQUID PHASE DATA FROM DIFFERENTIAL LIBERATION @ 157°F
0.88U 4~ 0.84 I
-; 0.80 I"(i5
~ 0.760a 0.72
OBR Fluid Properties Inc.
0.68 I I I I I
0 1000 2000 3000 4000 5000-0I-C/)
@)
""6>-0>--
LL>LL
(5
1.5oaR Fluid Properties Inc.
1.4
1.3
1.2
1.1~
1.0 I I I I I
0 1000 2000 3000 4000 5000
5.0
44.0 I
oaR Fluid Properties Inc.a::-u-->-
"(j)0ucn
::;:
(5
3.0
2.0
1.00.0 I I I I I I
0 1000 2000 3000 4000 5000
Pressure (psia)
DBRFPI-407109A MC291, Well #1: 11,456 Interval -Black Oil Study, 22
TABLE 4.5TEXACO -MISSISSIPPI CANYON 291, Well #1 :
DIFFERENTIAL LIBERATION VAPOR COMPOS1TIONS @ 157°F
COMPONENT MW 3500 psia 2000 psia 1000 psia 300 psiamole %
85 psia 15.025psia
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00331.00345.00359.00374.00388.00402.00580.00
0.0900.0000.398
93.6372.4731.5990.2700.6780.2250.2660.1930.0400.0040.0150.0640.0240.0040.0200.0010.0000.0000.0010.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.0970.0000.295
93.8442.6081.5320.2370.5780.1850.2200.1740.0410.0040.0180.0920.0250.0060.0210.0030.0060.0010.0040.0030.0020.0020.0010.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
17.78
0.106
0.1140.0000.181
92.9883.2321.8670.2660.6350.1810.2080.1440.0330.0060.0140.0550.0250.0040.0190.0020.0070.0000.0060.0060.0040.0020.0010.0010.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
17.93
0.047
0.1560.0000.076
86.8055.6673.9340.5631.3650.3720.4240.2780.0640.0070.0290.1080.0450.0070.0490.0040.0110.0010.0090.0110.0060.0050.0020.0010.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
19.75
0.015
0.2050.0000.300
70.34910.0729.5521.5073.8061.0721.2340.8030.1930.0230.0840.3770.1250.0250.1650.0050.0160.0020.0340.0220.0150.0090.0060.0020.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
25.75
0.004
0.2540.0000.406
33.97616.22516.12510.4929.4733.0983.6952.5810.6320.0730.2701.2660.4180.0830.5650.0510.0640.0090.1380.0660.0210.0130.0050.0020.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
40.07
0.001Density (g/cm3)
17.86
0.181
DBRFPI -407109A MC291. Well #1: 11.456 Interval- Black Oil Studv. 23
CO2H2SN2C1C2C3I-C4N-C4I-CSN-CSC6MCYC-CSBENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEO-XYLENEC9C10C11C12C13C14C1SC16C17C18C19C20C21C22C23C24C2SC26C27C28C29C30+
MW (Ib/lbmole)
TABLE 4.6TEXACO -MISSISSIPPI CANYON 291, Well #1: 11,456 ft INTERVAL:
MPSR 380: C30+ COMPOSITION OF D.L. RESIDUAL LIQUID
LIQUIDWT%
GROUPMOLE %COMPONENT MW MOLE %
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00331.00345.00359.00374.00388.00402.00580.00
0.0000.0000.0000.0000.0000.0320.0320.1380.1640.2490.7380.2180.0280.1841.1630.5130.1441.9010.0980.3660.1522.0393.2623.2233.2213.6833.4563.6163.9923.0763.6003.0212.8302.6662.5782.2052.3592.0331.9121.7941.7201.909
35.684
0.0000.0000.0000.0000.0000.1880.1430.6130.5850.8892.2040.6670.0930.5752.9891.3440.4014.2850.2390.8870.3684.0936.2675.6455.1505.4194.6834.5204.6293.3413.6932.9572.6492.3582.1761.7851.8351.5171.3711.2351.1411.223
15.840
0.0000.0000.0000.0000.0000.1880.1430.6130.5850.889
3.540
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEO-XYLENEC9C10C11C12C13C14C15C16C17C18C19C20C21C22C23C24C25C26C27C28C29C30+
14.606
27.164
19.141
17.29115.840
257.529.4
MW (Ib/lbmole)API GRAVITY °API
MC291, Well #1: 11,456 Interval- Black Oil Study, 24DBRFPI -407109A
TABLE 4.7
TEXACO -MISSISSIPPI CANYON 291, Well #1 :MPSR 380,11,456 ft INTERVAL: SEPARATOR TEST
Property Stage #11200 psia, 100°F
Stage #2250 psia, 75°F
Stage #315.025 psia, 75°F
Vapor Volume
(cm3)
60.25 38.60 284.04
Liquid Volume
( cm3)
42.80 40.54 40.15
Vapor Density(g/cm3)
0.072 0.015 0.001
Liquid Density(g/cm3)
0.825 0.862 0.871
GOR1 804
~1.071
86 38
'..,1.005
~1.015Separator
Volume Facto~
SEPARATOR SUMMARY DATA
Total Separator Gas-Oil Ratio1 (scf/bbl) 928
Separator Stock Tank Oil Gravity at GO°F 30.1
Separator Formation Volume Factor(bbl Reservoir Oil @ 157°F, 5150 psia / bbl STO @ 60OF) 1.414
1. Standard Cubic Feet of Gas I bbl of Oil @ 15.025 psia and GO°F2. bbl of Oil at P,T per bbl of STO @ 15.025 psia, GO°F
DBRFPI-407109A MC291, Well #1: 11,456 Interval- Black Oil Study, 25
TABLE 4.8TEXACO -MISSISSIPPI CANYON 291, Well #1: 11,456 ft INTERVAL:
MPSR 380 SEPARATOR TEST LIQUID COMPOSITION (1200 psia, 100°F)
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEO-XYLENEC9C10C11 .
C12C13C14C15C16C17C18C19C20C21C22C23C24C25C26C27C28C29C30+
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00331.00345.00359.00374.00388.00402.00580.00
0.3420.0000.340
63.11113.56011.1772.3364.7741.3671.3440.9030.1510.0440.0700.2600.0850.0270.0810.0060.0140.0020.0060.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.0000.0000.0000.0000.0000.0330.0330.1430.1690.2570.7620.2250.0290.1901.2020.5300.1481.9640.1020.3780.1572.1073.3703.3303.3283.8063.5713.7374.1253.1783.7213.1222.9242.7542.6642.2792.4372.1011.9761.8541.7771.972
33.540
0.0290.0000.0181.9610.7900.9860.2950.6730.3520.4320.8730.2380.0340.1911.1900.5180.1461.8800.0980.3610.1491.9993.1943.1563.1543.6073.3853.5423.9093.0123.5262.9592.7712.6112.5252.1602.3101.9911.8731.7571.6841.869
31.789
0.1160.0000.116
21.4994.6193.9330.8912.0370.8571.0521.7820.4980.0770.4092.0880.9280.2782.8940.1620.5980.2462.7404.1923.7763.4453.6253.1333.0233.0972.2352.4701.9781.7721.5781.4561.1941.2271.0150.9170.8260.7630.8189.638
26.96 252.80 175.850.825 g/cm:$ @ 100°F & 1200 psia
35 (M3/M3) 198 (SCF/STB)TABLE 4.9
TEXACO -MISSISSIPPI CANYON 291, Well #1: 11,456 ft INTERVAL:
0.1160.0000.116
21.4994.619
.3.9330.8912.0370.8571.052
2.766
9.934
18.171
12.804
11.5679.638
MW (Ib/lbmole) =DENSITY =GaR @ STD
DBRFPI-407109A MC291, Well #1: 11,456 Interval- Black Oil Study, 26
MPSR 380 SEPARATOR TEST VAPOR COMPOSITION (1200 psia, 100°F)
44.0134.0828.0116.0430.0744.0958.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00331.00345.00359.00374.00388.00402.00580.00
0.6320.0001.437
84.4288.7952.5840.5260.7630.2510.2060.2140.0310.0260.0120.0280.0350.0140.0130.0000.0000.0000.0050.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.2510.0000.898
92.1305.1201.0260.1580.2300.0610.0500.0430.0060.0060.0030.0050.0060.0030.0020.0000.0000.0000.0010.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.2510.0000.898
92.1305.1201.0260.1580.2300.0610.050
0.058
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEO-XYLENEC9C10C11C12C13C14C15C16C17C18C19C20C21C22C23C24C25C26C27C28C29C30+
0.017
0.0000.000
MW (Ib/lbmole)DENSITY (gicm3)
17.510.072
TABLE 4.10TEXACO -MISSISSIPPI CANYON 291, Well #1: 11,456 ft INTERVAL:
MPSR 380 SEPARATOR TEST LIQUID COMPOSITION (250 psia, 75°F)
MC291 , Well #1: 11,456 Interval- Black Oil Study, 27DBRFPI- 407109A
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEa-XYLENEC9C10C11C12C13C14C15C16C17C18C19C20C21C22C23C24C25C26C27C28C29C30+
44.0134.0828.0116.0430.0744.1058.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00331.00345.00359.00374.00388.00402.00580.00
0.3720.0002.271
45.15419.04318.5233.4286.4251.5741.4840.9380.1530.0460.0710.2660.0880.0300.0880.0030.0170.0020.0200.0030.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.0000.0000.0000.0000.0000.0330.0330.1410.1670.2530.7500.2220.0290.1871.1830.5210.1461.9330.1000.3720.1542.0733.3163.2773.2743.7453.5143.6774.0583.1273.6613.0712.8772.7102.6212.2422.3982.0671.9441.8241.7491.941
34.612
0.0130.0000.0500.5670.4490.6720.1880.4300.2510.3310.7950.2260.0310.1871.1750.5150.1451.8930.0980.3640.1502.0243.2353.1963.1943.6533.4273.5863.9583.0503.5702.9962.8062.6432.5562.1872.3392.0161.8961.7791.7051.893
33.760
0.0630.0000.3867.6783.2383.3070.7021.6050.7560.9962.0020.5840.0860.4932.5451.1390.3413.5970.2000.7450.3083.4255.2404.7194.3064.5313.9163.7793.8702.7943.0882.4732.2151.9721.8191.4931.5341.2691.1461.0320.9541.022
12.635
0.0630.0000.3867.6783.2383.3070.7021.6050.7560.996
3.165
12.298
22.711
16.003
14.45612.635
MW (Ib/lbmole) =DENSITY =GaR @ STD
31.44 255.090.862 g/cm;$ @ 75°F & 250 psi a
8 (M3/M3)
217.07
45 (SCF/STB)
MC291, Well #1: 11 ,456 Interval- Black Oil Study, 28DBRFPI-407109A
I
TABLE 4.11TEXACO -MISSISSIPPI CANYON 291, Well #1: 11,456 1t INTERVAL:
MPSR 380 SEPARATOR TEST VAPOR COMPOSITION (250 psia, 75°F)
44.0134.0828.0116.0430.0744.0958.1258.1272.1572.1586.2084.1678.1182.15
100.2098.1992.14
114.23106.17106.17106.17128.30134.00147.00161.00175.00190.00206.00222.00237.00251.00263.00275.00291.00305.00318.00331.00345.00359.00374.00388.00402.00580.00
0.7550.0000.184
55.52418.18713.8222.9474.3761.3561.0850.9200.1470.1320.0590.1660.1390.0550.1020.0070.0220.0040.0100.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
0.3740.0000.143
75.52513.1986..8401.1071.6430.4100.3280.2330.0380.0370.0150.0360.0310.0130.0190.0010.0040.0010.0020.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.0000.000
o.o.O.
75.13.6.1.1.O.O.
0.324
CO2H2SN2C1C2C3I-C4N-C4I-C5N-C5C6MCYC-C5BENZENECYCL-C6C7MCYCL-C6TOLUENEC8C2-BENZENEM&P-XYLENEO-XYLENEC9C10C11C12C13C14C15C16C17C18C19C20C21C22C23C24C25C26C27C28C29C30+
0.108
0.0000.000
MW (Ib/lbmole)DENSITY (g/cm3)
21.820.015
DBRFPI-407109A MC291, Well #1: 11 ,456 Interval- Black Oil Study, 29
374000143525198840107643410328
TABLE 4.12
TEXACO -MISSISSIPPI CANYON 291, Well #1 :
MPSR 380, 11,456 ft INTERVAL:SEPARATOR ADJUSTED SOLUTION GAS GOR AND FVF DATA
BASED ON DIFFERENTIAL LIBERATION @ 157°F
Pressure(psia)
Separator CorrectedSolution Gas
GOR (Rs)1
SeparatorCorrected
FVF (Bol
5150
3500
2000
1000
300
85
15.025
B.P. 928
512
268
130
25
1.414
1.262
1.161
1.106
1.066
1.057
1.035
Notes:
1. Rs = RSSb -(RsDb -RsD)(BoSb I BODb)
2. Bo = BoD (BoSb I BoDb)
where Rs -Separator Corrected Solution Gas GaR
Bo -Separator Corrected FVF
RsD -Gas in Solution at Specified Pressure
RsSb -Gas in Solution at Saturation by Separator Test
RsDb -Gas in Solution at Saturation by Differential Liberation
BoD -FVF at Specified Pressure
BOSb -FVF at Saturation from Separator Test
BoDb -FVF at Saturation from Differential Liberation
MC291, Well #1: 11,456 Interval -Black Oil Study, 30DBRFPI- 407109A
TABLE 5.1
BLACK OIL STUDY SUMMARY INFORMATION
Gas-Oil Ratio;(1)Total Solution Gas
Typeof
Liberation
Stock Tank OilGravity('API)
Formation VolumeFactor (2)
Reservoir Oil:
AtmosphericFlash @ 75°F
967 28.1 1.433
DifferentialLiberation@ 157°F
958 29.4 1.419
Two-StageSeparator Flash 928 30.1 1.414
Notes:
(1) Gas-Oil Ratio: SCF of Gas per bbl STO at GO°F
(2) Volume of Reservoir Oil @ 5150 psia, 157°F per volume STO @ 15.025 psia, GO°F
MC291, Well #1: 11 ,456 Interval- Black Oil Study, 33DBRFPI-407109A