Problem #2:
Given the following data:
Volume of bulk oil zone = 112,000 acre-ft
Volume of bulk gas zone = 19,600 acre-ft
Initial reservoir pressure = 2710 psia
Initial oil FVF = 1.340 bbl/STB
Initial gas FVF = 0.006266 ft3/SCF
Initial dissolved GOR = 562 SCF/STB
Oil produced during the interval = 20 MM STB
Reservoir pressure at the end of the interval = 2000
psia
Average produced GOR = 700 SCF/STB
Two-phase FVF at 2000 psia = 1.4954 bbl/STB
Volume of water encroached = 11.58 MM bbl
Volume of water produced = 1.05 MM STB
Water FVF = 1.028 bbl/STB
Gas FVF at 2000 psia = 0.008479 ft3/SCF
a) Calculate the
stock tank oil initially in place.
b) Calculate the
driving indexes.
c) Discuss your
results.
Solution:
a) The material
balance equation is written as:
Define the ratio of the initial gas cap volume to the
initial oil volume as:
we get:
and solve for N, we get:
Since:
Np =
20 x 106 STB
Bt =
1.4954 bbl/STB
Rp =
700 SCF/STB
Rsoi =
562 SCF/STB
Bg =
0.008479 ft3/SCF = 0.008479/5.6146 = 0.001510 bbl/SCF
We =
11.58 x 10 6 bbl
Wp =
1.05 x 106 STB
Bw =
1.028 bbl/STB
Bti =
1.34 bbl/STB
m = GBgi/NBti
= 19,600/112,000 = 0.175
Bgi =
0.006266 ft3/SCF = 0.006266/5.6146 = 0.001116 bbl/SCF
Thus:
b) In terms of
drive indexes, the material balance equation is written as:
Thus the depletion drive index (DDI) is given by:
The segregation drive index (SDI) is given by:
The water drive index (WDI) is given by:
c) The drive
mechanisms as calculated in part (b) indicate that when the reservoir pressure
has declined from 2710 psia to 2000 psia, 45% of the total production was by
oil expansion, 31% was by water drive, and 24% was by gas cap expansion.
Problem
#3: A plug, which has a length of 3.0 inches, a
diameter of 0.75 of an inch, was 100% saturated with water and placed in a
liquid permeameter. The water has a viscosity of 0.5 cp. The linear flow rate
was measured at 2.75 cc/sec with a pressure drop of 2.4 atm:
A. Calculate the absolute permeability.
B. If the plug was 100% saturated with a 5 cp oil, calculate the volume
flow rate when other parameters are kept the same.
Problem #4:
Given the following data:
Initial bulk reservoir volume = 415.3 MM ft3
Average porosity = 0.172
Average connate water saturation = 0.25
Initial pressure = 3200 psia
Initial gas FVF, Bgi = 0.005262 ft3/SCF
Final pressure = 2925 psia
Gas FVF at final pressure = 0.0057 ft3/SCF
Cumulative water production = 15,200 STB
Water FVF, Bw = 1.03 bbl/STB
Cumulative gas produced, Gp = 935.4 MM SCF
Bulk volume invaded by water at final pressure = 13.04
MM ft3
A) Calculate
initial gas in place.
B) Calculate
water influx, We.
C) Calculate
residual gas saturation, Sgr.
Solution:
A) G = 415.3 x 106
x 0.172 x (1 - 0.25) / 0.005262 = 10.18 MMM SCF
B) Since:
Rearranging and solving for We, we get:
which yields:
We = 935.4x106x0.0057 +
15,200x5.6146x1.03 - 10.18x109x(0.0057-0.005262)
= 960,400 ft3
C) Sw
= water volume/pore volume = Vw/Vp =
(connate
water + water influx - water produced)/pore volume =
(13.04x106x0.172x0.25
+ 960,400 - 15,200x5.6146x1.03)/
13.04x106x0.172
= 0.64
Therefore, Sgr = 1 - 0.64 = 0.36 or 36%.
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