natural gas assignment 6
TRANSCRIPT
![Page 1: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/1.jpg)
King Fahd University of Petroleum & Minerals
PETROLEUM ENGINEERING
PETE 544
NATURAL GAS ENGINEERING
Home Work #6
Prepared by:
Kareem Lateef Adewale
ID: g201004040
![Page 2: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/2.jpg)
QUESTION1
FLOW-AFTER-FLOW TEST DATA,QUESTION1
q(MMscf /D)
T(0F)
ptf
( psia)pwf
( psia)m( pwf )
( psia2/cp)
0 75 375.2 p=407.60 1.6173×107
4.288 70 371.2 403.13 1.5817×107
9.265 73 361.3 393.03 1.5032×107
15.552 77 343.8 375.79 1.3736×107
20.177 77 327.1 359.87 1.2591×107
Use P squared and pseudo – pressure to conduct analysis and determine the corresponding Rawlins-Schellhardt and Houpeurt’s equations. In both cases, determine the AOFP and use the Jones-Blount-Glaze method to determine effect of non-Darcy flow and the attainable increase in AOFP for a 20% increase in perforation interval.
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Solution1
PRESSURE SQUARED APPROACH
For Rawlins-Schellhardt analysis,
By graph
FLOW-AFTER-FLOW TEST DATA,QUESTION1
Nq
(MMscf /D)p2−pwf
2
( psia2 )1 4.288 3.869×103
2 9.265 1.191×104
3 15.552 2.516×104
4 20.177 3.688×104
1 10 100100
1000
10000
100000
f(x) = 465.83728062444 x^1.45469384554378R² = 0.999994565673201
(pi^2-pwf^2) versus q
pi^2-pwf^2Power (pi^2-pwf^2)
q (MMscf/day)
(p^2
-pw
f^2)
in (p
sia^2
)
![Page 4: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/4.jpg)
From the plot,
p2−pwf2 =465.8q1.454
Hence,
q=( p2−pwf
2
465.8 )(1
1.454 )=0.01462× ( p2−pwf
2 )0.6878
n=0.6878
C=0.01462(MMscf /D)/ psia1.3756
The absolute open flow potential (AOFP)
AOFP=C (p2 )n=0.01462×407.62×0.6878=56.96 MMscf /D
To use least square method
N log q log ( p2−pwf2 ) ( log q ) (log ( p2−pwf
2 )) (log ( p2−pwf2 ) )2
1 0.632255 3.587555298 2.268249 12.870553022 0.966845 4.07590553 3.940771 16.613005893 1.191786 4.400784611 5.244795 19.366905194 1.304857 4.566743725 5.958946 20.85514825
∑❑ 4.095743 16.63098916 17.41275982 69.70561234
for a least square fit of y=mx+c ,
m=N∑ ( xy )i−(∑ x i ) (∑ y i)N∑ (xx )i−(∑ x i ) (∑ x i )
∧c=(∑ y i ) (∑ ( xx )i)−(∑ ( xy )i )(∑ x i )
N∑ (xx )i−(∑ x i ) (∑ x i )
In our case, we are seeking,
log q=n log ( p2−pwf2 )+ logC
We have,
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n=N∑ ( (log q ) (log ( p2−pwf
2 ) ))i−(∑ log ( p2−pwf2 )i ) (∑ log q i)
N∑ ((log ( p2−pwf2 ) )2)i−(∑ log ( p2−pwf
2 )i ) (∑ log ( p2−pwf2 )i )
n= 4×17.41275982−16.63098916×4.0957434×69.70561234−16.63098916×16.63098916
=1.5347818452.23264892
=0.6874
C=10( (∑ log qi) (∑ (( log ( p2−pwf
2 ))2)i )−(∑ ( (log q )(log (p2−pwf2 ) ) )i) (∑ log (p2−pwf
2 )i )N∑ (( log ( p2−pwf
2 ))2 )i−(∑ log ( p2−pwf2 )i) (∑ log ( p2−pwf
2 )i) )
C=10( 4.095743×69.70561234−17.41275982×16.63098916
4× 69.70561234−16.63098916×16.63098916 )=10
(−4.095146012.23264892 )
=10−1.834209567=0.01465
Hence,
n=0.6874∧C=0.01465(MM scf /D)/ psia1.3748
The absolute open flow potential (AOFP)
AOFP=C (p2 )n=0.01465×407.62× 0.6874=56.81MMscf /D
For Houpeurt’s analysis
FLOW-AFTER-FLOW TEST DATA,QUESTION1
Nq
(MMscf /D)p2−pwf
2
( psia2 )1 4.288 3.869×103
2 9.265 1.191×104
3 15.552 2.516×104
4 20.177 3.688×104
Direct quadratic fit.
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2 4 6 8 10 12 14 16 18 20 220
5000
10000
15000
20000
25000
30000
35000
40000
f(x) = 51.6148925081009 x² + 795.386856513018 xR² = 0.999821333669731
(pi^2-pwf^2) versus q
pi^2-pwf^2Polynomial (pi^2-pwf^2)
q (MMscf/day)
(p^2
-pw
f^2)
in (p
sia^2
)
From the plot,
p2−pwf2 =795.3q+41.41q2
A=795.3 psia2/(MMscf /D)∧B=41.41 psia2/ (MMscf /D)2
The absolute open flow potential (AOFP)
AOFP=−A+√A2+4B PR
2
2B=−795.3+√795.32+4×41.41×407.602
2×41.41
¿ −795.3+5305.882.82
=54.46 MMscf /D
Using straight lines analysis.
FLOW-AFTER-FLOW TEST DATA,QUESTION1
Nq
(MMscf /D)
p2−pwf2
q( psia2 )/(MMscf /D)
1 4.288 902.19521922 9.265 1285.4645553 15.552 1618.073939
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4 20.177 1827.625172
2 4 6 8 10 12 14 16 18 20 220
200
400
600
800
1000
1200
1400
1600
1800
2000
f(x) = 57.6131633177468 x + 698.516742659067R² = 0.987019784874327
(pi^2-pwf^2)/(q) versus q
(pi^2-pwf^2)/(q)Linear ((pi^2-pwf^2)/(q))
q (MMscf/day
(p^2
-pw
f^2)
/q in
(psia
^2)/
(MM
scf/
D)
From the plot,
p2−pwf2 =698.5q+57.61q2
A=698.5 psia2/(MMscf /D)∧B=57.61 psia2/(MMscf /D)2
Using least square with straight line analysis
Np2−pwf
2
q( psia2 )/(MMscf /D)
q(MMscf /D)
p2−pwf2
( psia2 )q2
(MMscf /D)2
1 902.1952192 4.288 3.869×103 1.839×101
2 1285.464555 9.265 1.191×104 8.584×101
3 1618.073939 15.552 2.516×104 2.419×102
4 1827.625172 20.177 3.688×104 4.071×102
∑❑ 5633.358885 49.282 7.782×104 7.532×102
for a least squ are fit of y=mx+c ,
![Page 8: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/8.jpg)
m=N∑ ( xy )i−(∑ x i ) (∑ y i)N∑ (xx )i−(∑ x i ) (∑ x i )
∧c=(∑ y i ) (∑ ( xx )i)−(∑ ( xy )i )(∑ x i )
N∑ (xx )i−(∑ x i ) (∑ x i )
But we seek
p2−pwf2
q=A+Bq
Hence we have,
B=N∑ ( p2−pwf
2 )i−(∑ qi )(∑ ( p2−pwf
2
q )i)
N∑ (q2 )i−(∑ q i ) (∑ q i )=4×7.782×104−49.282×5633.358885
4×7.532×102−49.282×49.282
B=33656.80743584.084476
=57.623 psia2/ (MMscf /D)2
A=(∑( p
2−pwf2
q )i) (∑ (q2 )i )−(∑ ( p2−pwf
2 )i ) (∑ q i )
N∑ (q2 )i−(∑ q i )(∑ q i )
¿ 5633.358885×7.532×102−7.782×104×49.2824×7.532×102−49.282×49.282
=407920.6722584.084476
¿698.393 psia2/(MMscf /D)
The absolute open flow potential (AOFP)
AOFP=−A+√A2+4B PR
2
2B=−698.393+√698.3932+4×57.623×407.602
2×57.623
¿ −698.393+6227.4535115.246
=47.976 MMscf /D
If the perforation interval is increased by 20%,
B2=B1( hp1
hp2)
2
=57.623÷1.22=40.016 psia2/(MMscf /D)2
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AOFP2=−A+√A2+4 B2PR
2
2B2
=−698.393+√698.3932+4×40.016×407.602
2×40.016
¿ −698.393+5203.88680.032
=56.296 MMscf /D
AOFP2
AOFP1
=56.29647.976
=1.1734→17.34 %increase
PSEUDO-PRESSURE APPROACH
For Rawlins-Schellhardt analysis,
By graph
FLOW-AFTER-FLOW TEST DATA,QUESTION1
Nq
(MMscf /D)m (pR )−m( pwf )
( psia2/cp)1 4.288 3.560×105
2 9.265 1.141×106
3 15.552 2.437×106
4 20.177 3.582×106
The graph gives
![Page 10: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/10.jpg)
1 10 10010000
100000
1000000
10000000
f(x) = 40900.4099302299 x^1.49003637371691R² = 0.999942246527064
delta(m(p)) versus q
delta(m(p))Power (delta(m(p)))
m (pR )−m( pwf )=40900q1.49
q=(m ( pR )−m( pwf )40900 )(
11.49 )
=0.0008033× (m ( pR )−m( pwf ))0.6711
Then we have
n=0.6711
C=0.0008033(MMscf /D)/ (psia2/cp)0.6711
![Page 11: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/11.jpg)
To use least square method
N log q log (m ( pR )−m( pwf )) (log q ) (log (m ( pR )−m( pwf ))) (log (m ( pR )−m( pwf )))21 0.632255 5.551449998 3.509931 30.81862 0.966845 6.057285644 5.856459 36.690713 1.191786 6.386855529 7.611767 40.791924 1.304857 6.554125582 8.552194 42.95656
∑❑ 4.095743 24.54971675 25.53035 151.2578
for a least square fit of y=mx+c ,
m=N∑ ( xy )i−(∑ x i ) (∑ y i)N∑ (xx )i−(∑ x i ) (∑ x i )
∧c=(∑ y i ) (∑ ( xx )i)−(∑ ( xy )i )(∑ x i )
N∑ (xx )i−(∑ x i ) (∑ x i )
In our case, we are seeking,
log q=n log (m ( pR )−m(pwf ))+ logC
We have,
n=N∑ ( (log q ) (log (m ( pR )−m( pwf ))) )i−(∑ log (m ( pR )−m( pwf ))i ) (∑ log qi )
N∑ ((log (m ( pR )−m( pwf )))2)i−(∑ log (m ( pR )−m( pwf ))i ) (∑ log (m (pR )−m( pwf ))i )n= 4×25.53035−24.54971675×4.095743
4×151.2578−24.54971675×24.54971675=1.572069469
2.342607495=0.6711
C=10( (∑ log qi) (∑ (( log (m (p R)−m (pwf ) ))2 )i)−(∑ ( ( logq ) ( log (m (p R)−m (pwf ) )) )i) (∑ log (m (pR )−m( pwf ))i)
N∑ (( log (m (pR )−m( pwf )) )2)i−(∑ log (m ( pR)−m ( pwf) )i) (∑ log (m ( pR)−m (pwf ) )i) )
C=10( 4.095743×151.2578−25.53035× 24.54971675
4× 151.2578−24.54971675×24.54971675 )=10
(−7.2497854832.342607495 )
¿10−3.0947504=0.0008040(MMscf /D)/(psia2/cp )0.6711
The absolute open flow potential (AOFP)
AOFP=C (m ( pR ) )n=0.0008040× (1.6173×107 )0.6711=55.34 MMscf /D
![Page 12: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/12.jpg)
For Houpeurt’s analysis
FLOW-AFTER-FLOW TEST DATA,QUESTION1
Nq
(MMscf /D)m (pR )−m( pwf )
( psia2/cp)1 4.288 3.560×105
2 9.265 1.141×106
3 15.552 2.437×106
4 20.177 3.582×106
Direct quadratic fit.
![Page 13: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/13.jpg)
2 4 6 8 10 12 14 16 18 20 2210000
510000
1010000
1510000
2010000
2510000
3010000
3510000
4010000
f(x) = 5202.59272468827 x² + 73578.0737905572 xR² = 0.999761750934136
delta(m(p)) versus q
delta(m(p))Polynomial (delta(m(p)))
From the graph we have
m (pR )−m (pwf )=73578q+4059q2
A=73578( psia2/cp)/(MMscf /D)∧B=4059( psia2/cp)/(MMscf /D)2
Using straight lines analysis.
FLOW-AFTER-FLOW TEST DATA,QUESTION1
Nq
(MMscf /D)
m ( pR )−m(pwf )q
( psia2/cp)/(MMscf /D)1 4.288 8.302×104
![Page 14: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/14.jpg)
2 9.265 1.232×105
3 15.552 1.567×105
4 20.177 1.775×105
2 4 6 8 10 12 14 16 18 20 220
20000
40000
60000
80000
100000
120000
140000
160000
180000
200000
f(x) = 5875.49220204257 x + 62711.7499309184R² = 0.984253209643146
delta(m(p))/q
delta(m(p))/qLinear (delta(m(p))/q)
m (pR )−m (pwf )=62712q+5875q2
A=62712( psia2/cp)/(MMscf /D)∧B=5875 (psia2/cp) /(MMscf /D)2
Using least square with straight line analysis
Nm ( pR )−m ( pwf )
q( psia2/cp)/(MMscf /D)
q(MMscf /D)
m (pR )−m( pwf )( psia2/cp)
q2
(MMscf /D)2
![Page 15: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/15.jpg)
1 8.302×104 4.288 3.560×105 1.839×101
2 1.232×105 9.265 1.141×106 8.584×101
3 1.567×105 15.552 2.437×106 2.419×102
4 1.775×105 20.177 3.582×106 4.071×102
∑❑ 5.404×105 49.282 7.516×106 7.532×102
for a least square fit of y=mx+c ,
m=N∑ ( xy )i−(∑ x i ) (∑ y i)N∑ (xx )i−(∑ x i ) (∑ x i )
∧c=(∑ y i ) (∑ ( xx )i)−(∑ ( xy )i )(∑ x i )
N∑ (xx )i−(∑ x i ) (∑ x i )
But we seek
m ( pR )−m(pwf )q
=A+Bq
Hence we have,
B=N∑ (m (pR )−m( pwf ))i−(∑ qi )(∑(m ( pR )−m( pwf )
q )i)
N∑ (q2 )i−(∑ qi ) (∑ qi )= 4×7.516×106−49.282×5.404 ×105
4 ×7.532×102−49.282×49.282
B= 3432007.2584.084476
=5875.875( psia2/cp)/ (MMscf /D)2
A=(∑(m ( pR )−m( pwf )
q )i)(∑ (q2) i)−(∑ (m ( pR )−m( pwf ))i ) (∑ q i )
N∑ (q2 )i−(∑ qi ) (∑ qi )
¿ 5.404×105×7.532×102−7.516×106×49.2824×7.532×102−49.282×49.282
= 36625768584.084476
¿62706.3( psia2/cp)/ (MMscf /D)
The absolute open flow potential (AOFP)
AOFP=−A+√A2+4Bm ( pR )
2B=−62706.3+√62706.32+4×5875.875×1.6173×107
2×5875.875
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¿ −62706.3+619777.9411751.75
=47.403 MMscf /D
If the perforation interval is increased by 20%,
B2=B1( hp1
hp2)
2
=5875.875÷1.22=4080.469 (psia2/cp) /(MMscf /D)2
AOFP2=−A+√A2+4 B2m ( pR )
2B2
=−62706.3+√62706.32+4×4080.469×1.6173×107
2×4080.469
¿ −62706.3+517596.14038160.938
=55.740 MMscf /D
AOFP2
AOFP1
=55.74047.403
=1.1759→17.59%increase
QUESTION2
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For the modified isochronal test data shown in Table, determine the stabilized deliverability equation using both Rawlins and Schellhardt equation and Houpeurt’s equation, using the m(p)-approach. In addition, determine AOFP in each case. Make sure that you specify the units for all your final answers.
ISOCHRONAL TEST DATA,QUESTION2
NTime
(hours )q
(MMscf /D)pwf
( psia)
m (pwf )
( psia2
cp )1
0.5 0.983 344.7 9.6386×106
1.0 0.977 342.4 9.5406×106
2.0 0.970 339.5 9.4179×106
3.0 0.965 337.6 9.3381×106
2
0.5 2.631 329.5 9.0027×106
1.0 2.588 322.9 8.7351×106
2.0 2.533 315.4 8.4371×106
3.0 2.500 310.5 8.2458×106
3
0.5 3.654 318.7 8.5674×106
1.0 3.565 309.7 8.2071×106
2.0 3.453 298.6 7.7922×106
3.0 3.390 291.9 7.5435×106
4
0.5 4.782 305.5 8.0534×106
1.0 4.625 293.6 7.6136×106
2.0 4.438 279.6 7.0990×106
3.0 4.318 270.5 6.7797×106
214Extended flow point
1.156 291.6 7.5285×106
ps=352.4 psia,m (ps )=9.9715×106( psia2
cp )
Solution
For time = 0.5hrs
![Page 18: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/18.jpg)
Nq
(MMscf /D)pwf
( psia)
m (pwf )
( psia2
cp )∆ m ( p )
( psia2
cp )1 0.983 344.7 9.6386×106 3.33×105
2 2.631 329.5 9.0027×106 9.69×105
3 3.654 318.7 8.5674×106 1.40×106
4 4.782 305.5 8.0534×106 1.92×106
For time = 1hr
Nq
(MMscf /D)pwf
( psia)
m (pwf )
( psia2
cp )∆ m ( p )
( psia2
cp )1 0.977 342.4 9.5406×106 4.31×105
2 2.588 322.9 8.7351×106 1.24×106
3 3.565 309.7 8.2071×106 1.76×106
4 4.625 293.6 7.6136×106 2.36×106
For time = 2hrs
Nq
(MMscf /D)pwf
( psia)
m (pwf )
( psia2
cp )∆ m ( p )
( psia2
cp )1 0.970 339.5 9.4179×106 5.54×105
2 2.533 315.4 8.4371×106 1.53×106
3 3.453 298.6 7.7922×106 2.18×106
4 4.438 279.6 7.0990×106 2.87×106
For time = 3hrs
Nq
(MMscf /D)pwf
( psia)
m (pwf )
( psia2
cp )∆ m ( p )
( psia2
cp )1 0.965 337.6 9.3381×106 6.33×105
2 2.500 310.5 8.2458×106 1.73×106
3 3.390 291.9 7.5435×106 2.43×106
4 4.318 270.5 6.7797×106 3.19×106
Stabilized q(MMscf /D)
pwf
( psia)m (pwf ) ∆ m ( p )
![Page 19: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/19.jpg)
( psia2
cp ) ( psia2
cp )1 1.156 291.6 7.5285×106 2.443×106
Using the graph (R awlins and Schellhardt analysis .)
0.1 1 10100000
1000000
10000000
f(x) = 654208.237953186 x^1.07565751109846R² = 0.999722876065583f(x) = 569443.700547306 x^1.08130378434957R² = 0.999830816049961f(x) = 440808.496334169 x^1.09174396673275R² = 0.999952785937263f(x) = 337416.768473889 x^1.10337924882755R² = 0.999811599141631
Chart Titledelta(m(p )), t=0.5Power (delta(m(p )), t=0.5)delta(m(p )), t=1.0Power (delta(m(p )), t=1.0)delta(m(p )), t=2Power (delta(m(p )), t=2)delta(m(p )), t=3Power (delta(m(p )), t=3)delta(m(p )), stabilized
From the graph shown,
For t=0.5hrs we have
∆ m ( p )=33741q1.103 , n0.5=1
1.103=0.9066
For t=1hr we have
∆ m ( p )=44080q1.091 , n1.0=1
1.091=0.9166
For t=2hrs we have
![Page 20: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/20.jpg)
∆ m ( p )=56944 q1.081 ,n2.0=1
1.081=0.9251
For t=3hrs we have
∆ m ( p )=65420q1.075 , n3.0=1
1.075=0.9302
The value of n
n=n0.5+n1.0+n2.0+n3.0
4=0.9066+0.9166+0.9251+0.9302
4=0.9196
Using the stabilized flow result,
C= q
(∆m (p ) )n= 1.156
( 2.443×106 )0.9196=1.544×
10−6(MMscfD )
( psia2
cp )0.9196
Using least square with the power law (R awlins and Schellhardt analysis .)
For time = 0.5hrs
N log q log (∆m ( p ) ) ( log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 −0.00745 5.522314 −0.04112 30.495952 0.420121 5.986234 2.514942 35.8353 0.562769 6.147398 3.459562 37.79054 0.67961 6.282871 4.269899 39.47447
∑❑ 1.655052 23.93882 10.20328 143.5959
n0.5=N∑ ( (log q ) ( log (∆m (p ) ) ))i−(∑ log (∆m ( p )) i) (∑ log q i )N∑ ( ( log (∆m (p ) ) )2 )i−(∑ log (∆m (p ) )i )(∑ log (∆m ( p ) )i )
n0.5=4×10.20328−23.93882×1.6550524×143.5959−23.93882×23.93882
=1.1931280811.31497008
=0.9063
![Page 21: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/21.jpg)
For time = 1hrs
N log q log (∆m ( p ) ) (log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 −0.01011 5.634376 −0.05694 31.74622 0.412964 6.092159 2.515844 37.11443 0.55206 6.246597 3.448493 39.019974 0.665112 6.372525 4.238441 40.60908
∑❑ 1.62003 24.34566 10.14584 148.4897
n1.0=N∑ ( ( log q ) ( log (∆m ( p )) ))i−(∑ log (∆m ( p ) )i ) (∑ log q i)N∑ ( ( log (∆m (p ) ) )2 )i−(∑ log (∆m ( p )) i) (∑ log (∆m ( p ) )i )
n1.0=4×10.14584−24.34566×1.620034×148.4897−24.34566×24.34566
= 1.142660431.247639164
=0.9159
For time = 2hrs
N log q log (∆m ( p ) ) ( log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 −0.01323 5.743196 −0.07597 32.98432 0.403635 6.185939 2.496862 38.265843 0.538197 6.338317 3.411261 40.174264 0.647187 6.45826 4.179704 41.70912
∑❑ 1.575791 24.72571 10.01185 153.1335
n2.0=N∑ ( (log q ) ( log (∆m (p ) ) ))i−(∑ log (∆m ( p ) ) i) (∑ log q i)N∑ ( ( log (∆m (p ) ) )2 )i−(∑ log (∆m ( p ) )i) (∑ log (∆m ( p ) )i )
n2.0=4×10.01185−24.72571×1.5757914×153.1335−24.72571×24.72571
=1.0848487131.173264996
=0.9246
For time = 1hrs
![Page 22: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/22.jpg)
N log q log (∆m ( p ) ) (log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 −0.01547 5.801678 −0.08977 33.659472 0.39794 6.236965 2.481938 38.899743 0.5302 6.385249 3.385457 40.77144 0.635283 6.504036 4.131901 42.30248
∑❑ 1.54795 24.92793 9.909528 155.6331
n3.0=N∑ ( ( log q ) ( log (∆m ( p )) ))i−(∑ log (∆m ( p ) )i ) (∑ log q i)N∑ ( ( log (∆m (p ) ) )2 )i−(∑ log (∆m ( p )) i) (∑ log (∆m ( p ) )i )
n3.0=4×9.909528−24.92793×1.547954×155.6331−24.92793×24.92793
=1.0509227571.130705915
=0.9294
n=n0.5+n1.0+n2.0+n3.0
4=0.9063+0.9159+0.9246+0.9294
4=0.9191
Using the stabilized flow result,
C= q
(∆m (p ) )n= 1.156
( 2.443×106 )0.9191=1.555×
10−6(MMscfD )
( psia2
cp )0.9191
The absolute open flow potential (AOFP)
AOFP=C (m ( pR ) )n=1.555×10−6× (9.9715×106 )0.9191=4.21 MMscf /D
Using graph with Houpeurt’s analysis
![Page 23: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/23.jpg)
0.5 1 1.5 2 2.5 3 3.5 4 4.5 5100000
600000
1100000
1600000
2100000
2600000
3100000
3600000
f(x) = 25892.0971806497 x² + 627504.330509668 xR² = 0.999997509536971
f(x) = 21203.5411198209 x² + 554355.462625557 xR² = 0.999985289566808
f(x) = 16489.070435942 x² + 434387.183540542 xR² = 0.999986302982386
f(x) = 15578.9632718121 x² + 326857.10451369 xR² = 0.99999739986266
Chart Titledelta(m(p )), t=0.5Polynomial (delta(m(p )), t=0.5)delta(m(p )), t=1.0Polynomial (delta(m(p )), t=1.0)delta(m(p )), t=2Polynomial (delta(m(p )), t=2)delta(m(p )), t=3
From the graph above we have,
when t=0.5hrsm ( pR )−m ( pwf )=326857q+14519q2
when t=1hrsm ( pR )−m ( pwf )=434,387q+13284 q2
when t=2hrsm ( pR )−m ( pwf )=554355q+19051q2
when t=3hrsm ( pR )−m ( pwf )=627504q+27131q2
The average value of B
B=14519+13284+19051+271314
=18496 ( psia2/cp)/(MMscf /D)2
From the stabilized test,
A=∆m ( p )−Bq2
q=2.443×106−18496×1.156
1.165=2,094,826( psia2/cp)/(MMscf /D)
![Page 24: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/24.jpg)
The absolute open flow potential (AOFP)
AOFP=−A+√A2+4Bm ( pR )
2B=−2,094,826+√2,094,8262+4 ×18496×9.9715×106
2×18496
¿ −2,094,826+619777.9436992
=4.58 MMscf /D
N q ∆ m ( p ) ∆m (p )q
(q )2
1 0.983 3.33×105 3.39×105 0.9662892 2.631 9.69×105 3.68×105 6.9221613 3.654 1.40×106 3.84×105 13.3517164 4.782 1.92×106 4.01×105 22.867524
∑❑ 12.05 4.62×106 1.49×106 44.10769
B0.5=N∑ (∆m ( p ) )i−(∑ q i)(∑ (∆m ( p )
q )i)
N∑ (q2 )i−(∑ q i) (∑ q i)
¿4 ( 4.62×106 )−12.05 ( 1.49×106 )
4 ( 44.10769 )−12.052 =16827.7( psia2/cp)/ (MMscf /D)2
N q ∆ m ( p ) ∆m (p )q
(q )2
1 0.977 4.31×105 4.41×105 0.9545292 2.588 1.24×106 4.78×105 6.6977443 3.565 1.76×106 4.95×105 12.7092254 4.625 2.36×106 5.10×105 21.390625
∑❑ 11.755 5.79×106 1.92×106 41.752123
B1=N∑ (∆m (p ) )i−(∑ qi )(∑ (∆ m ( p )
q )i)
N∑ (q2 )i−(∑ qi ) (∑ qi )
¿4 (5.79×106 )−11.755 ( 1.92×106 )
4 (41.752123 )−11.7552 =20479.8( psia2/cp)/(MMscf /D)2
![Page 25: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/25.jpg)
N q ∆ m ( p ) ∆m (p )q
(q )2
1 0.97 5.54×105 5.71×105 0.94092 2.533 1.53×106 6.06×105 6.4160893 3.453 2.18×106 6.31×105 11.9232094 4.438 2.87×106 6.47×105 19.695844
∑❑ 11.394 7.14×106 2.45×106 38.976042
B2=N∑ (∆m (p ) )i−(∑ qi )(∑ (∆ m ( p )
q )i)
N∑ (q2 )i−(∑ qi ) (∑ qi )
¿4 (7.14 ×106 )−11.394 (2.45×106 )
4 (38.976042 )−11.3942 =24719.2( psia2/cp)/(MMscf /D)2
N q ∆ m ( p ) ∆m (p )q
(q )2
1 0.965 6.33×105 6.56×105 0.9312252 2.500 1.73×106 6.90×105 6.25003 3.39 2.43×106 7.16×105 11.49214 4.318 3.19×106 7.39×105 18.645124
∑❑ 11.173 7.98×106 2.80×106 37.318449
B3=N∑ (∆m (p ) )i−(∑ qi ) (∑ ( ∆m ( p )
q )i)
N∑ (q2 )i−(∑ qi ) (∑ qi )
¿4 (7.98×106 )−11.173 (2.80×106 )
4 (37.318449 )−11.1732 =26008.8 (psia2/cp )/(MMscf /D)2
B=B0.5+B1+B2+B3
4=16827.7+20479.8+24719.2+26008.8
4=22008.9 ( psia2/cp )/(MMscf /D)2
Using the stabilized flow data
![Page 26: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/26.jpg)
A=∆m ( p )
q−Bq=2.443×106
1.156−22008.9×1.156=2.1133×106−2.5442×104=2.09×106( psia2/cp)/(MMscf /D)
The absolute open flow potential (AOFP)
AOFP=−A+√A2+4Bm ( pR )
2B=
−2.09×106+√ (2.09×106 )2+4×22008.9×9.9715×106
2×22008.9=4.55MMscf /D
QUESTION3
For the modified isochronal test data shown in Table 7.15, determine the stabilized deliverability equation using both Rawlins and Schellhardt equation and Houpeurt’s equation, using the m(p)-approach. In addition, determine AOFP in each case. Make sure that you specify the units for all your final answers.
MODIFIED ISOCHRONALTEST DATA
Time(hours )
Pwf ( psia)
q=1.520 MMscf /D q=2.041 MMscf /D q=2.688 MMscf /D q=3.122 MMscf /D0(Pwf ) 706.6 706.6 703.5 701.2
0 .5 655.6 624.5 578.5 541.71 .0 653.6 620.7 573.9 537.81 .5 652.1 619.9 572.3 536.32 .0 651.3 619.1 570.8 534.7
m (Pwf ) ( psia2/cp )0(m(Pwf )) 5.093×107 5.093×107 5.093×107 5.015×107
0 .5 4.379×107 3.970×107 3.403×107 2.979×107
1 .0 4.352×107 3.922×107 3.348×107 2.936×107
1 .5 4.332×107 3.911×107 3.330×107 2.919×107
2 .0 4.321×107 3.901×107 3.312×107 2.902×107
Extended Flow pointPwf=567.7 psia t=24hoursP=706.6 psia q=2.665 MMscf /D
m (Pwf )=3.276×107 psia2/cp m (14.65 )=2,766.6 psia2/cp
For t=0.5hr
![Page 27: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/27.jpg)
N q (MMscf /D) ∆ m ( p )1 1.52 7.14×106
2 2.041 1.12×107
3 2.688 1.69×107
4 3.122 2.04×107
For t=1hr
N q (MMscf /D) ∆ m ( p )1 1.52 7.41×106
2 2.041 1.17×107
3 2.688 1.75×107
4 3.122 2.08×107
For t=1.5hrs
N q (MMscf /D) ∆ m ( p )1 1.52 7.61×106
2 2.041 1.18×107
3 2.688 1.76×107
4 3.122 2.10×107
For t=2.0hrs
N q (MMscf /D) ∆ m ( p )1 1.52 7.72×106
2 2.041 1.19×107
3 2.688 1.78×107
4 3.122 2.11×107
Rawlins and Schellhardt
Direct plot
From the plot below,
n=n0.5+n1.0+n1.5+n2.0
4=0.681+0.690+0.702+0.706
4=0.695
For stabilized condition,
![Page 28: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/28.jpg)
∆ m ( p )=1.817×107
C= 2.665
(1.817×107 )0.695=2.401×10−5 (MMscf /D ) / (psia2/cp )0.695
The absolute open flow potential (AOFP)
AOFP=C (m ( pR ) )n=2.401×10−5× (5.093×107 )0.695=5.454 MMscf /D
50000000.04
0.4
4
f(x) = 2.06471560745552E-05 x^0.706254075283929R² = 0.998371809142411
f(x) = 2.20556050369769E-05 x^0.702675892049939R² = 0.998332432684058
f(x) = 2.69949669815724E-05 x^0.690939724313441R² = 0.997841306338301
f(x) = 3.23427450024902E-05 x^0.681291681662476R² = 0.998819511063778
Chart Title
q(t=0.5)Power (q(t=0.5))q(t=1.0)Power (q(t=1.0))q(t=1.5)Power (q(t=1.5))
N log q log (∆m ( p ) ) (log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 0.181843588 6.853698212 1.246301074 46.973179182 0.309843005 7.050379756 2.184510848 49.707854713 0.429429264 7.227886705 3.103866071 52.24234621
![Page 29: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/29.jpg)
4 0.494432899 7.308777774 3.613700181 53.41823254
∑❑ 1.415548756 28.44074245 10.14837817 202.3416126
n0.5=N∑ ( (log q ) ( log (∆m (p ) ) ))i−(∑ log (∆m ( p )) i) (∑ log q i )N∑ ( ( log (∆m (p ) ) )2 )i−(∑ log (∆m (p ) )i )(∑ log (∆m ( p ) )i )
¿ 4×10.14837817−28.44074245×1.415548756
4×202.3416126−28.440742452=0.681292
\
N log q log (∆m ( p ) ) (log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 0.181843588 6.869818208 1.249232391 47.194402212 0.309843005 7.068556895 2.190142907 49.964496583 0.429429264 7.241795431 3.109838885 52.443601074 0.494432899 7.317854489 3.618188008 53.55099433
∑❑ 1.415548756 28.49802502 10.16740219 203.1534942
n1=N∑ (( log q ) (log (∆m ( p ) ) ) )i−(∑ log (∆m ( p ) )i ) (∑ log qi )N∑ ( ( log (∆m ( p ) ) )2)i−(∑ log (∆m ( p ) )i ) (∑ log (∆m (p ) )i )
¿ 4×10.16740219−28.49802502×1.415548756
4×203.1534942−28.498025022=0.69094
N log q log (∆m ( p ) ) (log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 0.181843588 6.881384657 1.251335676 47.353454792 0.309843005 7.072617477 2.19140105 50.021917973 0.429429264 7.246252312 3.1117528 52.508172574 0.494432899 7.321391278 3.619936712 53.60277025
∑❑ 1.415548756 28.52164572 10.17442624 203.4863156
n1.5=N∑ ( ( log q ) ( log (∆m ( p )) ))i−(∑ log (∆m ( p ) )i ) (∑ log q i)N∑ ( ( log (∆m (p ) ) )2 )i−(∑ log (∆m ( p )) i) (∑ log (∆m ( p ) )i )
¿ 4×10.17442624−28.52164572×1.415548756
4×203.4863156−28.521645722=0.702676
N log q log (∆m ( p ) ) (log q ) ( log (∆ m ( p ) ) ) ( log (∆m (p ) ) )21 0.181843588 6.8876173 1.252469042 47.43927208
![Page 30: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/30.jpg)
2 0.309843005 7.076276255 2.192534697 50.073685643 0.429429264 7.250663919 3.113647273 52.572127274 0.494432899 7.324899497 3.621671291 53.65415264
∑❑ 1.415548756 28.53945697 10.1803223 203.7392376
n2=N∑ (( log q ) (log (∆m ( p ) ) ) )i−(∑ log (∆m ( p ) )i ) (∑ log qi )N∑ ( ( log (∆m ( p ) ) )2 )i−(∑ log (∆m ( p ) )i ) (∑ log (∆m (p ) )i )
¿ 4×10.1803223−28.53945697×1.4155487564×203.7392376−28.53945697
=0.706254
n=n0.5+n1.0+n1.5+n2.0
4=0.681292+0.69094+0.702676+0.706254
4=2.781161
4=0.69529
For stabilized condition,
∆ m ( p )=1.817×107
C= 2.665
(1.817×107 )0.69529=2.39×10−5 (MMscf /D )/( psia2/cp)0.69529
The absolute open flow potential (AOFP)
AOFP=C (m ( pR ) )n=2.39×10−5× (5.093×107 )0.69529=5.46 MMscf /D
Houpeurt’s
Direct quadratic fit
![Page 31: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/31.jpg)
1.4 1.6 1.8 2 2.2 2.4 2.6 2.8 3 3.2 3.40.00E+00
5.00E+06
1.00E+07
1.50E+07
2.00E+07
2.50E+07
f(x) = 988961.882938625 x² + 3776831.7852842 xR² = 0.999522288207357f(x) = 1008628.50557362 x² + 3672867.58705707 xR² = 0.999594709709602f(x) = 1030594.46284472 x² + 3555151.89000456 xR² = 0.999431404206438f(x) = 1088225.65468236 x² + 3220036.88613934 xR² = 0.999664805244604
Chart Title delta m(p)Polynomial (delta m(p))delta m(p)Polynomial (delta m(p))delta m(p)
B=B0.5+B1+B2+B3
4=988,962+1,088,226+1,030,594+1,008,629
4=1029103( psia2/cp)/(MMscf /D)2
A=∆m ( p )
q−Bq=1.817×107
2.665−1029103×2.665=4.075×106( psia2/cp)/(MMscf /D)
The absolute open flow potential (AOFP)
AOFP=−A+√A2+4Bm ( pR )
2B=
−4.075×106+√( 4.075×106 )2+4×1029103×5.093×107
2×1029103
¿5.32 MMscf /D
Least square.
Nq ∆ m ( p ) ∆m (p )
q(q )2
1 1.52 7.14×106 4.70×106 2.31042 2.041 1.12×107 5.49×106 4.1656813 2.688 1.69×107 6.29×106 7.2253444 3.122 2.04×107 6.53×106 9.746884
∑❑ 9.371 55640000 23006349.83 23.448309
![Page 32: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/32.jpg)
B0.5=N∑ (∆m ( p ) )i−(∑ q i)(∑ (∆m ( p )
q )i)
N∑ (q2 )i−(∑ q i) (∑ q i)
¿4 (55640000 )−9.371 (23006349.83 )
4 (23.448309 )−9.3712=1,165,602( psia2/cp)/(MMscf /D)2
N q ∆ m ( p ) ∆m (p )q
(q )2
1 1.52 7.41×106 4.88×106 2.31042 2.041 1.17×107 5.73×106 4.1656813 2.688 1.75×107 6.51×106 7.2253444 3.122 2.08×107 6.66×106 9.746884
∑❑ 9.371 57410000 23780296.64 23.448309
B1=N∑ (∆m (p ) )i−(∑ qi )(∑ (∆ m ( p )
q )i)
N∑ (q2 )i−(∑ qi ) (∑ qi )
¿4 (57410000 )−9.371 (23780296.64 )
4 (23.448309 )−9.3712=1,136,718 (psia2/cp) /(MMscf /D)2
N q ∆ m ( p ) ∆m (p )q
(q )2
1 1.52 7.61×106 5.01×106 2.31042 2.041 1.18×107 5.78×106 4.1656813 2.688 1.76×107 6.55×106 7.2253444 3.122 2.10×107 6.73×106 9.746884
∑❑ 9.371 58010000 24062135.06 23.448309
B1 .5=N∑ (∆m (p ) )i−(∑ qi )(∑( ∆m ( p )
q )i)
N∑ (q2 )i−(∑ qi ) (∑ qi )
¿4 (58010000 )−9.371 (24062135.06 )
4 (23.448309 )−9.3712=1,096,383( psia2/cp)/(MMscf /D)2
![Page 33: Natural Gas Assignment 6](https://reader033.vdocuments.site/reader033/viewer/2022061107/544bc50eaf7959a0438b56ba/html5/thumbnails/33.jpg)
N q ∆ m ( p ) ∆m (p )q
(q )2
1 1.52 7.72×106 5.08×106 2.31042 2.041 1.19×107 5.83×106 4.1656813 2.688 1.78×107 6.62×106 7.2253444 3.122 2.11×107 6.76×106 9.746884
∑❑ 9.371 58520000 24289934.58 23.448309
B2.0=N∑ (∆ m ( p ) )i−(∑ q i)(∑ (∆m ( p )
q )i)
N∑ (q2 )i−(∑ qi ) (∑ qi )
¿4 (58520000 )−9.371 (24289934.58 )
4 (23.448309 )−9.3712=1,080,539( psia2/cp)/(MMscf /D)2
B=B0.5+B1+B2+B3
4=1,165,602+1,136,718+1,096,383+1,080,539
4
¿1,119,810.5 (psia2/cp) /(MMscf /D)2
A=∆m ( p )
q−Bq=1.817×107
2.665−1,119,810.5×2.665=3.834×106( psia2/cp)/ (MMscf /D)
The absolute open flow potential (AOFP)
AOFP=−A+√A2+4Bm ( pR )
2B=
−3.834×106+√(3.834×106 )2+4 ×1,119,810.5×5.093×107
2×1,119,810.5
¿5.25 MMscf /D