data dan perhitungan ipr 3 fasa

8/16/2019 Data Dan Perhitungan IPR 3 fasa

1/30

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


2/30

#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


3/30

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


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


4/30

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


5/30

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


6/30

• 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

) ]


7/30

= 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"#


8/30

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


9/30

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"#


10/30

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

)


11/30

=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


12/30

15

Qw max

1283,6

6 bbl/d

Tabel 3.2.2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins


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


13/30

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


1174,

817

909,2

59

Tabel 3.2.). Perhitungan Qo, Qw, & Qt (ada !uture Pr %11' (si menggunakan Metode


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


14/30

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


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


15/30

0 500 1000 1500 2000 2500 3000

0

500

1000

1500

FIPR II

qw

qo

qt


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


16/30

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


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


17/30

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


904,1

44

401,4

35

Tabel 3.3.). Perhitungan Qo, Qw, & Qt (ada !uture Pr %11'' (si menggunakan Metode



18/30

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


19/30

Tabel 3.3.. Perhitungan Qo, Qw, & Qt (ada !uture Pr %'' (si menggunakan Metode


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


20/30

0 500 1000 1500 2000

0

100

200

300

400

500

600

700

800

FIPR II

qw

qo

qt


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


21/30

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


22/30

Tabel 3.).2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins


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


761,2

35

327,2

04

Tabel 3.).). Perhitungan Qo, Qw, & Qt (ada !uture Pr % '' (si menggunakan Metode


Pwf Qo Qw Qt


23/30

(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


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


24/30

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


25/30

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


26/30

Tabel 3..2. Perhitungan Qo, Qw & Qt Present menggunakan Metode IP 3 !asa Wiggins


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


552,6

05

239,4

96


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Tabel 3..). Perhitungan Qo, Qw, & Qt (ada !uture Pr % '' (si menggunakan Metode


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


Pwf (psi)

Qo(bbl/d)

Qw(bbl/d)

Qt(bbl/d)

500 0 0 0

400 136.800

58.62857

14 195


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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


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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


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data dan perhitungan ipr 3 fasa

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