Post on 05-Jul-2018
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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2.3. PERHITUNGAN
3.1. Well 1
a) Data
Tabel 3.1.1. Data Well 1
Qo 380 bbl/d
WC 22 %
GOR 300 scf/bbl
Pr 1275 Psi
Pwf 1200 Psi
Qw 107,18 bbl/d
GLR 234 scf/bbl
Qo max4449,7
57 bbl/d
Qw max1442,0
33 bbl/d
Tabel 3.1.2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins
dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1275 0 0 0
1200 380 107.179 487.179
1000
1321.0
70 379.331
1700.40
0
800
2157.0
29 631.612
2788.64
0
600
2887.8
77 864.022
3751.89
9
400
3513.6
14 1076.563
4590.17
7
200
4034.2
41 1269.233
5303.47
4
0
4449.7
57 1442.033
5891.79
0
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#ra"ik 3.1.1 Qo, Qw dan Qt
0 1000 2000 3000 4000 5000 6000 7000
0
200
400
600
800
1000
1200
1400
IPR
Qo
Qw
Qt
Q (bbl/day)
Pwf (psi)
Tabel 3.1.3. Perhitungan !uture Qo & Qw Ma$imum % 11' (si dan %1''' (si
Future Pr (psi) !" """Future Qo max
(bbl/d)3642,
847
2822,
798
Future Qw max(bbl/d)
1180,
538
914,7
85
Tabel 3.1.). Perhitungan Qo, Qw, & Qt (ada !uture Pr %11' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1150 0.000 0.000 0
900 1089.411 312.876 1402.287
800 1478.900 429.278 1908.178
700 1841.945 540.682 2382.627
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600 2178.547 647.086 2825.633
500 2488.705 748.492 3237.197
400 2772.420 844.899 3617.319
300 3029.692 936.307 3965.999
200 3260.520 1022.716 4283.237
100 3464.905 1104.126 4569.032
0 3642.847 1180.538 4823.385
#ra"ik 3.1.2. Qo, Qw, dan Qt (ada "uture Pr % 11' Psi
0.000 2000.000 4000.000 6000.000
0
200
400
600
800
1000
1200
1400
FIPR I
qwqo
qt
Tabel 3.1.. Perhitungan Qo, Qw, & Qt (ada !uture Pr %1''' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1000 0 0 0
800 781.351
223.9392
64 1005
600 1454.30 427.3873 1882
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6 53
4002018.86
5610.3442
68 2629
200
2475.03
0
772.8100
08 3248
0
2822.79
8
914.7845
74 3738
#ra"ik 3.1.2. Qo, Qw dan Qt (ada !uture P % 1''' Psi
0 500 1000 1500 2000 2500 3000 3500 4000
0
200
400
600
800
1000
1200
FIPR II
qw
qo
qt
Tabel 3.1.*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
Pwf (psi) Q(bbl/d)
Pre#uirm
e$t%ori&o$tal (psi)
OPR
'*!(i$+,)
-!(i$+,)
.!(i$+,)
1275 0.000 300
1200 487.179 300 911 825 744
1000
1700.40
0 300 1,076 947 839
800 2788.64 300 1,202 1019 888
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0
6003751.89
9 300 1,324 1079 924
400
4590.17
7 300 1,441 1131 952
200
5303.47
4 300 1,551 1178 975
0
5891.79
0 300 1648 1218 993
#ra"ik 3.1.3. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan
korelasi 0agedorn rown
0.000 2000.000 4000.000 6000.000
0
200
400
600
800
1000
1200
1400
/odal 0$alysis
IPR
2.875
3.5
4.5
FIPR I
FIPR II
b) Perhitungan
• Qo = 380 bbl/d
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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• WC = 22 %
• GOR = 300 scf/bbl
• Pr = 1275 psi
• Pwf = 1200 psi
Me!i"#! Qw $
• Qw =Qo
1−WC x WC
=380
1−0,22 x 0,22
= 1071! bbl"#
Me!i"#! G&R $
• G&R = GOR x (1−WC )
= 300 x (1−0,22 )
= 23$ %&'"bbl
Me!i"#! Qo '() d( Qw '() 'e!!#(*( Me"ode +PR 3 ,(s(
Wi!!is $
• Qo '() = [ Qo
(1−0,52 x( Pwf Pr )−0,48 x ( Pwf
Pr )2
) ]= [
380
(1−0,52 x(12001275 )−0,48 x (1200
1275 )2
) ]= $$$(77 bbl"#
• Qw '() = [ Qw
(1−0,72 x( Pwf Pr )−0,28 x ( Pwf
Pr )2
) ]
= [ 107,18
(1−0,72 x(12001275 )−0,28 x (1200
1275 )2
) ]
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= 1$$2033 bbl"#
Co"o c(r( 'e!i"#! Qo- Qw d( Q" 'e!!#(*( Me"ode +PR 3 ,(s(
Wi!!is de!( d("( Pwf (s#'si $
• Pwf .1275 psi
Qo =Qomax x (1−0,52 x ( Pwf Pr )−0,48 x (
Pwf
Pr )2
)
= -757 x (1−0,52 x (12751275 )−0,48 x (
1275
1275 )2
)
= 0 bbl"#
Qw =Qwmax x (1−0,72 x( Pwf Pr )−0,28 x ( Pwf Pr )
2
)
= 1442,033 x (1−0,72 x ( 12751275 )−0,28 x(12751275 )2
)
= 0 bbl"#
Q" = Qo Qw
= 0 bbl"#
• Pwf .800 psi
Qo =Qomax x (1−0,52 x ( Pwf Pr )−0,48 x (
Pwf
Pr )2
)
= -757 x (1−0,52 x ( 8001275 )−0,48 x ( 8001275 )
2
)
= 21702( bbl"#
Qw =Qwmax x (1−0,72 x( Pwf Pr )−0,28 x ( Pwf Pr )
2
)
= 1442,033 x (1−0,72 x ( 8001275 )−0,28 x(
800
1275 )2
)
= *31*12 bbl"#
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Q" = Qo Qw
=27!!*$0 bbl"#
Me!i"#! Qo '() d( Qw '() ,#"#re p(d( ,#"#re Pr .1150 d(
.1000 psi 'e!!#(*( Me"ode ,#"#re +PR 3 ,(s( Wi!!is$
• ,#"#re Pr .1150 psi
Qo '() f =Qomax p x (0,15 x( Pr f Pr p )+0,84 x ( Pr f Pr p )
2
)
= -757 x (0,15 x
(1150
1275
)+0,84 x
( 1150
1275
)
2
)
= 3*$2!$7 bbl"#
Qw '() f = Qwmax px (0,59 x ( Pr f Pr p )+0,36 x ( Pr f
Pr p )2
)
= 1442,033 x (0,59 x (11501275 )+0,36 x (
1150
1275 )2
)
= 11!03! bbl"#a+
• ,#"#re Pr .1000 psi
Qo '() f =Qomax p x (0,15 x( Pr f Pr p )+0,84 x (
Pr f
Pr p )2
)
= -757 x (0,15 x(10001275 )+0,84 x(
1000
1275 )2
)
= 2!227(! bbl"#
Qw '() f =Qwmax px (0,59 x ( Pr f Pr p )+0,36 x (
Pr f
Pr p )2
)
= 1442,033 x (0,59 x (10001275 )+0,36 x (
1000
1275 )2
)
= (1$7! bbl"#a+
Me!i"#! Qo- Qw d( Q" p(d( s((" ,#"#re Pr .1150 psi 'e!!#(*(
Me"ode +PR 3 ,(s( Wi!!is de!( d("( Pwf (s#'si $
• Pwf .1150 psi
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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Qo =Qomax f x (1−0,52 x( Pwf Pr )−0,48 x (
Pwf
Pr )2
)
= 32-87 x (1−0,52 x (11501150 )−0,48 x (
1150
1150 )2
)
= 0 bbl"#
Qw =Qwmaxf x (1−0,72 x ( Pwf Pr )−0,28 x ( Pwf Pr )
2
)
=1180,538 x (1−0,72 x (11501150 )−0,28 x (
1150
1150 )2
)
= 0 bbl"#
Q" = Qo Qw
= 0 bbl"#
• Pwf .00 psi
Qo = Qomax f x (1−0,52 x( Pw f
Pr )−0,48 x
( Pwf Pr )
2
)
= 32-87 x (1−0,52 x ( 4001150 )−0,48 x ( 4001150 )
2
)
= 2772$20 bbl"#
Qw =Qwmaxf x
(1
−0,72 x
( Pwf
Pr
)−0,28 x
( Pwf
Pr
)
2
)
= 1180,538 x (1−0,72 x ( 4001150 )−0,28 x (
400
1150 )2
)
= !$$!(( bbl"#
Q" = Qo Qw
= 3*1731( bbl"#
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Me!i"#! Qo- Qw d( Q" p(d( s((" ,#"#re Pr .1000 psi 'e!!#(*(
Me"ode +PR 3 ,(s( Wi!!is de!( d("( Pwf (s#'si $
• Pwf .1000 psi
Qo = Qomax f x (1−0,52 x( Pwf Pr )−0,48 x ( Pwf
Pr )2
)
= 2822-78 x (1−0,52 x (10001000 )−0,48 x (1000
1000 )2
)
= 0 bbl"#
Qw =Qwmaxf x (1−0,72 x ( Pwf Pr )−0,28 x ( Pwf Pr )
2
)
= 914,875 x (1−0,72 x(10001000 )−0,28 x (
1000
1000 )2
)
= 0bbl"#
Q" = Qo Qw
= 0 bbl"#
• Pwf .800 psi
Qo =Qomax f x (1−0,52 x ( Pwf Pr )−0,48 x (
Pwf
Pr )2
)
= 2822-78 x (1−0,52 x ( 8001000 )−0,48 x (
800
1000 )2
)
= 7!131 bbl"#
Qw =Qwmaxf x (1−0,72 x ( Pwf Pr )−0,28 x (
Pwf
Pr )2
)
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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=914,875 x (1−0,72 x( 8001000 )−0,28 x ( 8001000 )
2
)
= 223(3( bbl"#
Q" = Qo Qw
= 1002(0 bbl"#
Peri"#!( pee"#( OPR #"#* #*#r( "#bi! 2 7/8 3-5 4 -5 'e!!#(*(
*orel(si (!edor 6row
#ambar sheet hagedornbrown
3.2 Well 2
a) DataTabel 3.2.1. Data Well 2
Qo 375 bbl/d
WC 30 %
GOR 380 scf/bbl
Pr 1200 Psi
Pwf 1080 Psi
Qw 160,71 bbl/d
GLR 266 scf/bbl
Qo max 2618,7 bbl/d
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15
Qw max
1283,6
6 bbl/d
Tabel 3.2.2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins
dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1200 0 0 0
1000
611.03
35 263.864 874.897
800
1152.2
35 507.759
1659.99
4
600
1623.6
03 731.686
2355.29
0
400
2025.1
40 935.646
2960.78
5
200
2356.8
44 1119.637
3476.48
1
0
2618.7
15 1283.660
3902.37
6
3.2.1 gra"ik Qo, Qw dan Qt
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0 1000 2000 3000 4000 5000
0
200
400
600
800
1000
1200
1400IPR
Qo
Qw
Qt
Q (bbl/day)
Pwf (psi)
Tabel 3.2.3. Perhitungan !uture Qo & Qw Ma$imum % 11' (si dan %1''' (si
Future Pr (psi) !" """Future Qo max
(bbl/d)2396,
670
1854,
923
Future Qw max(bbl/d)
1174,
817
909,2
59
Tabel 3.2.). Perhitungan Qo, Qw, & Qt (ada !uture Pr %11' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1150 0 0 0
900 716.736 311.360 1028.095
800 972.985 427.198 1400.183
700 1211.836 538.062 1749.898
600 1433.290 643.951 2077.241
500 1637.347 744.865 2382.212
400 1824.006 840.805 2664.811
300 1993.268 931.770 2925.038
200 2145.133 1017.760 3162.893
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100 2279.600 1098.776 3378.376
0 2396.670 1174.817 3571.487
3.2.2 gra"ik Qo, Qw, dan Qt (ada "uture Pr % 11' Psi
0.000 2000.000 4000.000 6000.000
0
500
1000
1500
FIPR I
qw
qo
qt
Tabel 3.2.. Perhitungan Qo, Qw, & Qt (ada !uture Pr %1''' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1000 0 0 0
800 513.443
222.5867
18 736
600 955.656
424.8060
25 1380
400
1326.64
1
606.6579
19 1933
200
1626.39
7
768.1424
01 2395
0
1854.92
3
909.2594
71 2764
3.2.2 gra"ik Qo, Qw dan Qt (ada !uture P % 1''' Psi
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0 500 1000 1500 2000 2500 3000
0
500
1000
1500
FIPR II
qw
qo
qt
Tabel 3.2.*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
Pwf (psi) Q(bbl/d)
Pre#uirm
e$t%ori&o$tal (psi)
OPR
'*!(i$+,)
-!(i$+,)
.!(i$+,)
1200 0.000 300
1000 874.897 300 916 824 741
800
1659.99
4 300 1,007 887 788
600
2355.29
0 300 1,082 932 819
400
2960.78
5 300 1,150 968 842
200
3476.48
1 300 1,212 998 860
0
3902.37
6 300 1,265 1023 874
#ra"ik 3.2.3. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan
korelasi 0agedorn rown
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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0.000 1000.000 2000.000 3000.000 4000.000
0
200
400
600
800
1000
1200
1400odal 0$alysis
IPR
2.875
3.5
4.5
FIPR I
FIPR II
3.3 Well 3
a) DataTabel 3.3.1. Data Well 3
Qo 250 bbl/d
WC 19 %
GOR 290 scf/bbl
Pr 1250 Psi
Pwf 1200 Psi
Qw 58,64 bbl/d
GLR 234,9 scf/bbl
Qo max4278,4
78 bbl/d
Qw max1155,4
61 bbl/dTabel 3.3.2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins
dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1250 0 0 0
1200
250.00
0 58.642 308.642
1000 1184.2 282.857 1467.14
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83 0
8002013.4
17 490.5072503.92
5
600
2737.4
04 681.593
3418.99
7
400
3356.2
43 856.114
4212.35
7
200
3869.9
34 1014.070
4884.00
4
04278.4
78 1155.4615433.93
9
3.3.1 gra"ik Qo, Qw dan Qt
0 2000 4000 6000
0
500
1000
1500
IPR
Qo
Qw Qt
Q (bbl/day)
Pwf (psi)
Tabel 3.3.3. Perhitungan !uture Qo & Qw Ma$imum % 11'' (si dan %1''' (si
Future Pr (psi) "" *""Future Qo max
(bbl/d)3347,
892
1486,
446
Future Qw max(bbl/d)
904,1
44
401,4
35
Tabel 3.3.). Perhitungan Qo, Qw, & Qt (ada !uture Pr %11'' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1100 0 0 0
900
847.76361
64
202.05000
8 1049.814
800
1231.8027
48
296.79831
1 1528.601
700
1589.2800
96
387.36214
6 1976.642
600
1920.1956
59
473.74151
3 2393.937
500
2224.5494
37
555.93641
3 2780.486
400
2502.3414
32
633.94684
6 3136.288
300
2753.5716
42 707.77281 3461.344
200
2978.2400
68
777.41430
7 3755.654
100
3176.3467
09
842.87133
6 4019.218
0
3347.8915
66
904.14389
8 4252.035
3.3.2 gra"ik Qo, Qw, dan Qt (ada "uture Pr % 11'' Psi
0 1000 2000 3000 4000 5000
0
200
400
600
800
1000
1200
FIPR I
qw qo
qt
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Tabel 3.3.. Perhitungan Qo, Qw, & Qt (ada !uture Pr %'' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
700 0 0 0
600 299.716 71.111 371
500 570.310 137.635 708
400 811.781 199.571 1011
300
1024.13
1 256.918 1281
200
1207.35
8 309.678 1517
100
1361.46
3 357.851 1719
0
1486.44
6 401.435 1888
3.3.2 gra"ik Qo, Qw dan Qt (ada !uture P % 1''' Psi
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0 500 1000 1500 2000
0
100
200
300
400
500
600
700
800
FIPR II
qw
qo
qt
Tabel 3.3.*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
Pwf (psi) Q(bbl/d)
Pre#uirm
e$t%ori&o$tal (psi)
OPR
'*!(i$+,)
-!(i$+,)
.!(i$+,)
1250 0.000 300
1200 308.642 300 819 746 680
1000
1467.14
0 300 984 874 781
800
2503.92
5 300 1,092 940 826
600
3418.99
7 300 1,194 992 858
400
4212.35
7 300 1,292 1037 883
200 4884.00 300 1,382 1076 903
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4
05433.93
9 300 1461 1109 919
#ra"ik 3.3.3. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
0.000 1000.000 2000.000 3000.000 4000.000 5000.000
0
200
400
600
800
1000
1200
odal 0$alysis
IPR
2.875
3.5
4.5
FIPR I
FIPR II
3.$ Well $
a) DataTabel 3.).1. Data Well )
Qo 480 bbl/d
WC 35 %GOR 400 scf/bbl
Pr 900 Psi
Pwf 700 Psi
Qw 258,46 bbl/d
GLR 260 scf/bbl
Qo max1572,8
16 bbl/d
Qw max955,08
1 bbl/d
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Tabel 3.).2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins
dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
900 0 0 0
800
249.32
04 132.532 381.853
600
692.03
9 377.788
1069.82
7
400
1060.1
94 596.631
1656.82
5
200
1353.7
86 789.062
2142.84
9
0
1572.8
16 955.081
2527.89
7
#ra"ik 3.).1 Qo, Qw dan Qt
0 2000 4000
0
500
1000
IPR
Qo Qw Qt
Q (bbl/day)
Pwf (psi)
Tabel 3.).3. Perhitungan !uture Qo & Qw Ma$imum % '' (si dan % '' (si
Future Pr (psi) "" !""Future Qo max
(bbl/d)1253,
592
538,8
35
Future Qw max(bbl/d)
761,2
35
327,2
04
Tabel 3.).). Perhitungan Qo, Qw, & Qt (ada !uture Pr % '' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf Qo Qw Qt
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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(psi) (bbl/d) (bbl/d) (bbl/d)
800 0 0 0
700 222.513 118.467 340.980
600 426.221 230.274 656.495
500 611.126 335.419 946.546
400 777.227 433.904 1211.131
300 924.524 525.728 1450.252
200 1053.017 610.891 1663.909
100 1162.707 689.394 1852.100
0 1253.592 761.235 2014.827
#ra"ik 3.).2 Qo, Qw, dan Qt (ada "uture Pr % 11'' Psi
0 500 1000 1500 2000 2500
0
100
200
300
400
500
600
700
800
900
FIPR I
qw
qo qt
Tabel 3.).. Perhitungan Qo, Qw, & Qt (ada !uture Pr %'' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
500 0 0 0
400 149.150
80.09949
47 229
300 277.608 152.8696 430
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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24
200 385.375218.3103
87 604
100 472.450
276.4217
86 749
0 538.835
327.2038
18 866
#ra"ik 3.).2 Qo, Qw dan Qt (ada !uture P % 1''' Psi
0 200 400 600 800 1000
0
200
400
600
FIPR II
qw
qo qt
Tabel 3.).*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
Pwf (psi) Q
(bbl/d)
Pre#uirm
e$t%ori&o$tal (psi)
OPR
'*!(i$+,) -!(i$+,) .!(i$+,)
900 0.000 300
800 381.853 300 778 710 648
600
1069.82
7 300 873 785 707
400
1656.82
5 300 933 825 737
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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200
2142.84
9 300 980 854 756
0
2527.89
7 300 1,017 875 770
#ra"ik 3.).3. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
0.000 500.000 1000.000 1500.000 2000.000 2500.000
0
100
200
300
400
500
600
700
800
900
odal 0$alysis
IPR
2.875
3.5
4.5
FIPR I
FIPR II
3.$ Well
a) DataTabel 3..1. Data Well
Qo 480 bbl/d
WC 30 %
GOR 400 scf/bbl
Pr 1000 Psi
Pwf 800 Psi
Qw 205,71 bbl/d
GLR 280 scf/bbl
Qo max1734,1
04 bbl/d
Qw max840,33
6 bbl/d
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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Tabel 3..2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins
dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
1000 0 0 0
800
480.00
00 205.714 685.714
600
893.41
0 392.605
1286.01
5
400
1240.2
31 560.672
1800.90
3
200
1520.4
62 709.916
2230.37
8
0
1734.1
04 840.336
2574.44
0
#ra"ik 3..1 Qo, Qw dan Qt
0 2000 4000
0
1000
2000
IPR
Qo Qw Qt
Q (bbl/day)
Pwf (psi)
Tabel 3..3. Perhitungan !uture Qo & Qw Ma$imum % '' (si dan % '' (si
Future Pr (psi) "" !""Future Qo max
(bbl/d)1140,
347
494,2
2
Future Qw max(bbl/d)
552,6
05
239,4
96
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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Tabel 3..). Perhitungan Qo, Qw, & Qt (ada !uture Pr % '' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
800 0 0 0
600
387.71791
91
167.16302
5 554.881
400
707.01502
89
314.98487
4 1022.000
200
957.89132
95
443.46554
6 1401.357
0
1140.3468
21
552.60504
2 1692.952
#ra"ik 3..2 Qo, Qw, dan Qt (ada "uture Pr % 11'' Psi
0 200 400 600 800 1000 1200 1400 1600 1800
0
200
400
600
800
1000
FIPR I
qw
qo
qt
Tabel 3... Perhitungan Qo, Qw, & Qt (ada !uture Pr %'' (si menggunakan Metode
!uture IP 3 !asa Wiggins dengan data Pw" asumsi
Pwf (psi)
Qo(bbl/d)
Qw(bbl/d)
Qt(bbl/d)
500 0 0 0
400 136.800
58.62857
14 195
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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300 254.622
111.8924
37 367
200 353.466
159.7915
97 513
100 433.332
202.3260
5 636
0 494.220
239.4957
98 734
#ra"ik 3.).2 Qo, Qw dan Qt (ada !uture P % 1''' Psi
0 100 200 300 400 500 600 700 800
0
100
200
300
400
500
600
FIPR II
qwqo
qt
Tabel 3..*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
Pwf (psi) Q(bbl/d)
Pre#uirm
e$t%ori&o$tal (psi)
OPR
'*!(i$+,)
-!(i$+,)
.!(i$+,)
1000 0.000 300
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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800 685.714 300 905 816 736
6001286.01
5 300 984 875 781
400
1800.90
3 300 1,043 913 808
200
2230.37
8 300 1,091 941 828
0
2574.44
0 300 1,130 963 842
#ra"ik 3..3. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi
0agedorn rown
0.000 1000.000 2000.000 3000.0000
200
400
600
800
1000
1200
odal 0$alysis
IPR
2.875
3.5
4.5
FIPR I
FIPR II
8/16/2019 Data Dan Perhitungan IPR 3 fasa
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