Data Dan Perhitungan IPR 3 fasa

2.3. PERHITUNGAN 3.1. Well 1 a) Data Tabel 3.1.1. Data Well 1

Qo WC GOR Pr Pwf Qw GLR

380 380 22 300 300

Qo max Qw max

bbl/ bbl/d d % scf/bb scf/bbll

1275 1275

Psi

1200 1200

Psi

107, 107,18 18

bbl/d bbl/d

234 234 4449,7 57 1442,0 33

scf/bb scf/bbll bbl/ bbl/d d bbl/ bbl/d d

Tabel Tabel 3.1.2. Perhitungan Qo, Qw & Qt Present P resent menggunakan Metode IP I P 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

48 487.179

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

#ra"ik 3.1.1 Qo, Qw dan Qt

IPR 1400 1200 1000 Qo

800 800

Pwf (psi)

Qw

600 600

Qt

400 400 200 200 0 0

1000 1000 2000 2000 3000 3000 4000 4000 5000 5000 6000 6000 7000 7000

Q (bbl/day)

Tabel Tabel 3.1.3. Perhitungan !uture Qo & Qw M a$imum % 11' (si dan %1''' (si

Futur ture Pr (psi (psi)) Future Qo max (bbl/d) Future Qw max (bbl/d)

!" !"

""" """

3642, 847 1180, 538

2822, 798 914,7 85

Tabel Tabel 3.1.). Perhitungan Qo, Qw, Qw, & Qt (ada !uture Pr %11' %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

#ra"ik 3.1.1 Qo, Qw dan Qt

IPR 1400 1200 1000 Qo

800 800

Pwf (psi)

Qw

600 600

Qt

400 400 200 200 0 0

1000 1000 2000 2000 3000 3000 4000 4000 5000 5000 6000 6000 7000 7000

Q (bbl/day)

Tabel Tabel 3.1.3. Perhitungan !uture Qo & Qw M a$imum % 11' (si dan %1''' (si

Futur ture Pr (psi (psi)) Future Qo max (bbl/d) Future Qw max (bbl/d)

!" !"

""" """

3642, 847 1180, 538

2822, 798 914,7 85

Tabel Tabel 3.1.). Perhitungan Qo, Qw, Qw, & Qt (ada !uture Pr %11' %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

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

FIPR I 1400 1200 1000

qw

800 800

qo qt

600 600 400 400 200 200 0 0.000

2000.000

4000.000

6000.000

Tabel 3.1.. Perhitungan Qo, Qw, & Qt (ada !uture Pr %1''' (si menggunakan Metode !uture IP 3 !asa Wiggins 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

6

53

400

2018.86 5

610.3442 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

FIPR II 1200 1000

qw

800

qo qt

600 400 200 0 0

500 1000 1500 2000 2500 3000 3500 4000

Tabel 3.1.*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi 0agedorn rown

Pwf (psi)

Q (bbl/d)

P re#uirm e$t %ori&o$ tal (psi)

1275

0.000

300

1200

487.179

OPR '*! (i$+,)

-! (i$+,)

.! (i$+,)

300

911

825

744

1000

1700.40 0

300

1,076

947

839

800

2788.64

300

1,202

1019

888

0

600

3751.89 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

/odal 0$alysis 1400 1200

IPR 2.875

1000

3.5

800

4.5 FIPR I

600

FIPR II 400 200 0 0.000

b) Perhitungan Qo = 380 bbl/d •

2000.000

4000.000

6000.000

• • • •

WC = 22 % GOR = 300 scf/bbl Pr = 1275 psi Pwf = 1200 psi

Me!i"#! Qw $ •

Qw =

Qo x WC = 1 −WC

380 1 −0,22

x 0,22

= 1071! 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!!is $

•

Qo '() =

=

[ [

Qo

( )

Pwf ( 1−0,52 x Pr

( ) )

Pwf −0,48 x Pr

2

]

380

( 1−0,52 x

( )− 1200 1275

0,48 x

( )) 2

1200 1275

]

= $$$(77 bbl"#

•

Qw '() =

=

[ [

Qw

( )

Pwf ( 1−0,72 x Pr

( 1−0,72 x

( ) )

Pwf −0,28 x Pr

2

]

107,18

( )− 1200 1275

0,28 x

( )) 1200 1275

2

]

= 1$$2033 bbl"#

Co"o c(r( 'e!i"#! Qo- Qw d( Q" 'e!!#(*( Me"ode +PR 3 ,(s( Wi!!is de!( d("( Pwf (s#'si $ •

Pwf .1275 psi

( ) ( ) ( )− ( ) ) 2

Qo =

Pwf Pwf − 0,48 x ) Qomax x ( 1− 0,52 x Pr Pr

= -757

x ( 1−0,52 x

1275 1275

0,48 x

1275

2

1275

= 0 bbl"#

( ) ( ) ( )− ( ) ) 2

Qw =

=

Pwf Pwf −0,28 x ) Qwmax x ( 1−0,72 x Pr Pr 1275

1442,033 x ( 1 −0,72 x

1275

1275

0,28 x

2

1275

= 0 bbl"# Q" = Qo  Qw = 0 bbl"# •

Pwf .800 psi Qo =

( )

( )

2

Pwf − 0,48 x Pwf ) Qomax x ( 1− 0,52 x Pr Pr

= -757

x ( 1−0,52 x

( )− 800

1275

0,48 x

( )) 2

800

1275

= 21702( bbl"#

Qw =

( )

( )

2

Pwf Pwf −0,28 x ) Qwmax x ( 1−0,72 x Pr Pr

1442,033 x ( 1 −0,72 x =

= *31*12 bbl"#

( ) 800

1275

−0,28 x

( )) 800

1275

2

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!!is$ •

,#"#re Pr .1150 psi

( ) ( ) ( )+ ( ) ) 2

Qo '() f =

Pr f + 0,84 x Pr f ) Qomax p x ( 0,15 x Pr p Pr p 1150

( 0,15 x = -757 x 1275

0,84 x

1150

2

1275

= 3*$2!$7 bbl"#

( ) ( ) ( )+ ( ) ) 2

Qw '() f =

=

Pr f Pr f +0,36 x ) Qwmax px ( 0,59 x Pr p Pr p 1442,033

x ( 0,59 x

1150

1275

0,36 x

1150

2

1275

= 11!03! bbl"#a+

•

,#"#re Pr .1000 psi

( ) ( ) ( )+ ( ) ) 2

Qo '() f =

Pr f Pr f + 0,84 x ) Qomax p x ( 0,15 x Pr p Pr p

= -757

x ( 0,15 x

1000 1275

0,84 x

2

1000 1275

= 2!227(! bbl"#

( ) ( ) ( )+ ( ) ) 2

Qw '() f =

=

Pr f Pr f +0,36 x ) Qwmax px ( 0,59 x Pr p Pr p 1442,033

x ( 0,59 x

1000 1275

0,36 x

1000

2

1275

= (1$7! bbl"#a+ Me!i"#! Qo- Qw d( Q" p(d( s((" ,#"#re Pr .1150 psi 'e!!#(*( Me"ode +PR 3 ,(s( Wi!!is de!( d("( Pwf (s#'si $ Pwf .1150 psi •

Qo =

( )

( )

( )−

( ))

2

Pwf −0,48 x Pwf ) Qomax f x ( 1 −0,52 x Pr Pr

= 32-87

x ( 1−0,52 x

1150 1150

0,48 x

1150

2

1150

= 0 bbl"#

Qw =

=

( )

( )

( )−

( ))

2

Pwf − 0,28 x Pwf ) Qwmaxf x ( 1− 0,72 x Pr Pr 1180,538 x ( 1−0,72 x

1150 1150

0,28 x

2

1150 1150

= 0 bbl"# Q" = Qo  Qw = 0 bbl"# •

Pwf .00 psi Qo =

( )

( )

( )−

( ))

2

Pw f −0,48 x Pwf ) Qomax f x ( 1 −0,52 x Pr Pr 400

( 1−0,52 x = 32-87 x 1150

0,48 x

2

400

1150

= 2772$20 bbl"#

Qw =

=

( )

( )

( )−

( ))

2

Pwf − 0,28 x Pwf ) Qwmaxf x ( 1− 0,72 x Pr Pr 1180,538 x ( 1−0,72 x

= !$$!(( bbl"#

Q" = Qo  Qw = 3*1731( bbl"#

400

1150

0,28 x

400

1150

2

Me!i"#! Qo- Qw d( Q" p(d( s((" ,#"#re Pr .1000 psi 'e!!#(*( Me"ode +PR 3 ,(s( Wi!!is de!( d("( Pwf (s#'si $ Pwf .1000 psi • Qo =

( )

( )

( )−

( ))

2

Pwf Pwf −0,48 x ) Qomax f x ( 1 −0,52 x Pr Pr 1000

( 1−0,52 x = 2822-78 x 1000

0,48 x

1000

2

1000

= 0 bbl"# Qw =

=

( )

( )

( )−

( ))

2

Pwf Pwf − 0,28 x ) Qwmaxf x ( 1− 0,72 x Pr Pr 914,875 x ( 1−0,72 x

1000 1000

0,28 x

2

1000 1000

= 0bbl"#

Q" = Qo  Qw = 0 bbl"#

•

Pwf .800 psi Qo =

( )

( )

( )−

( ))

2

Pwf Pwf −0,48 x ) Qomax f x ( 1 −0,52 x Pr Pr

= 2822-78

x ( 1− 0,52 x

800

1000

0,48 x

800

1000

= 7!131 bbl"# Qw =

( )

( )

2

Pwf Pwf − 0,28 x ) Qwmaxf x ( 1− 0,72 x Pr Pr

2

=

914,875 x ( 1− 0,72 x

( )− 800

1000

0,28 x

( )) 800

2

1000

= 223(3( bbl"# Q" = Qo  Qw = 1002(0 bbl"# Peri"#!( pee"#( OPR #"#* #*#r( "#bi! 2 7/8 3-5 4 -5 'e!!#(*( *orel(si (!edor 6row

#ambar sheet hagedornbrown

3.2 Well 2 a) Data Tabel 3.2.1. Data Well 2

Qo WC GOR Pr Pwf Qw GLR Qo max

375 30 380

bbl/d % scf/bbl

1200

Psi

1080

Psi

160,71

bbl/d

266 2618,7

scf/bbl bbl/d

15 1283,6 6

Qw max

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

IPR 1400 1200 1000 800

Pwf (psi)

600

Qo

400

Qw

200

Qt

0 0

1000

2000

3000

4000

5000

Q (bbl/day)

Tabel 3.2.3. Perhitungan !uture Qo & Qw Ma$imum % 11' (si dan %1''' (si

Future Pr (psi) Future Qo max (bbl/d) Future Qw max (bbl/d)

!"

"""

2396, 670 1174, 817

1854, 923 909,2 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

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

FIPR I 1500

qw qo

1000

qt

500 0 0.000

2000.000

4000.000

6000.000

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

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

800

3.2.2 gra"ik Qo, Qw dan Qt (ada !uture P % 1''' Psi

FIPR II 1500 qw

1000

qo 500

qt

0 0

500

1000

1500

2000

2500

3000


Pwf (psi)

Q (bbl/d)


1200

0.000

300

1000

874.897

OPR '*! (i$+,)

-! (i$+,)

.! (i$+,)

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


odal 0$alysis 1400 1200 IPR 1000

2.875 3.5

800

4.5 FIPR I

600

FIPR II 400 200 0 0.000

1000.000

2000.000

3000.000

4000.000

3.3 Well 3 a) Data Tabel 3.3.1. Data Well 3

Qo WC GOR Pr Pwf Qw GLR

250 19 290

bbl/d % scf/bbl

1250

Psi

1200

Psi

58,64

bbl/d

234,9 scf/bbl 4278,4 78 bbl/d 1155,4 61 bbl/d

Qo max Qw max

Tabel 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

83

0

800

2013.4 17

490.507

2503.92 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

0

4278.4 78

1155.461

5433.93 9

3.3.1 gra"ik Qo, Qw dan Qt

IPR 1500 1000

Pwf (psi)

500 Qo 0

Qw 0

2000

4000

Qt

6000

Q (bbl/day)

Tabel 3.3.3. Perhitungan !uture Qo & Qw M a$imum % 11'' (si dan %1''' (si


""

*""

3347, 892 904,1 44

1486, 446 401,4 35

Tabel 3.3.). Perhitungan Qo, Qw, & Qt (ada !uture Pr %11'' (si menggunakan Metode !uture IP 3 !asa Wiggins dengan data Pw" asumsi

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

FIPR I 1200 1000 800 600

qw

400

qt

200 0 0

1000

2000

3000

4000

5000

qo

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

FIPR II 800 700 600 500 400

qw

300

qo

200

qt

100 0 0

500

1000

1500

2000


Pwf (psi)

Q (bbl/d)


1250

0.000

300

1200

308.642

OPR '*! (i$+,)

-! (i$+,)

.! (i$+,)

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

4

0

5433.93 9

300

1461

1109

919


odal 0$alysis 1200 1000

IPR 2.875

800

3.5 4.5

600

FIPR I FIPR II

400 200 0 0.000

1000.000 2000.000 3000.000 4000.000 5000.000

3.$ Well $ a) Data Tabel 3.).1. Data Well )

Qo WC GOR Pr Pwf Qw GLR Qo max Qw max

480 35

bbl/d %

400

scf/bbl

900

Psi

700

Psi

258,46

bbl/d

260 1572,8 16 955,08 1

scf/bbl bbl/d bbl/d

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

IPR 1000

Pwf (psi)

500 0 0

Qo

2000 4000

Qw

Qt

Q (bbl/day)

Tabel 3.).3. Perhitungan !uture Qo & Qw Ma$imum % '' (si dan % '' (si


""

!""

1253, 592 761,2 35

538,8 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

(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

FIPR I 900 800 700 600 500 400 300 200 100 0

qw qo

0

500

1000

1500

2000

qt

2500

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

24

200

100

0

385.375

218.3103 87

604

472.450

276.4217 86

749

538.835

327.2038 18

866

#ra"ik 3.).2 Qo, Qw dan Qt (ada !uture P % 1''' Psi

FIPR II 600 400 qw 200

qo

qt

0 0

200

400

600

800

1000

Tabel 3.).*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi 0agedorn rown

Pwf (psi)

Q (bbl/d)


900

0.000

300

800

381.853

OPR '*! (i$+,)

-! (i$+,)

.! (i$+,)

300

778

710

648

600

1069.82 7

300

873

785

707

400

1656.82 5

300

933

825

737

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

odal 0$alysis 900 800

IPR

700

2.875

600

3.5

500

4.5

400

FIPR I

300

FIPR II

200 100 0 0.000

500.000

1000.000 1500.000 2000.000 2500.000

3.$ Well  a) Data Tabel 3..1. Data Well 

Qo WC GOR Pr Pwf Qw GLR Qo max Qw max

480 30 400

bbl/d % scf/bbl

1000

Psi

800

Psi

205,71

bbl/d

280 1734,1 04 840,33 6

scf/bbl bbl/d bbl/d

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

IPR 2000

Pwf (psi)

1000 0 0

2000 4000

Qo

Qw

Qt

Q (bbl/day)

Tabel 3..3. Perhitungan !uture Qo & Qw Ma$imum % '' (si dan % '' (si


""

!""

1140, 347 552,6 05

494,2 2 239,4 96

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

FIPR I 1000 800

qw qo

600

qt

400 200 0 0

200

400

600

800 1000 1200 1400 1600 1800

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

136.800

58.62857 14

195

400

300

200

100

0

254.622

111.8924 37

367

353.466

159.7915 97

513

433.332

202.3260 5

636

494.220

239.4957 98

734

#ra"ik 3.).2 Qo, Qw dan Qt (ada !uture P % 1''' Psi

FIPR II 600 500

qw qo

400

qt

300 200 100 0 0

100

200

300

400

500

600

700

800

Tabel 3..*. Penentuan +P untuk ukuran tubing 2 -/ 3,/ & ), menggunakan korelasi 0agedorn rown

Pwf (psi)

Q (bbl/d)


1000

0.000

300

OPR '*! (i$+,)

-! (i$+,)

.! (i$+,)

800

685.714

300

905

816

736

600

1286.01 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

odal 0$alysis 1200 IPR

1000

2.875 800

3.5 4.5

600

FIPR I FIPR II

400 200 0 0.000

1000.000

2000.000

3000.000

Data Dan Perhitungan IPR 3 fasa

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