perhitungan mass flow.xlsx

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INPUT 80 MMscfd OUTPUT 143,174.72 lb/hr Komponen % Mol N2 0.12 CO2 0.33 CH4 98.77 C2H6 0.53 C3H8 0.23 iC4H10 0.02 nC4H10 0.01 iC5H10 0.00 nC5H10 0.00 C6H14 0.00 TOTAL 100 Komponen % M ol Nitrogen 0.5 CO2 5 Metana 88 Etana 4 Propana 1.5 i-Butana 0.6 n-Butana 0.4 TO TAL 100

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Page 1: Perhitungan Mass Flow.xlsx

INPUT 80 MMscfdOUTPUT 143,174.72 lb/hr

Komponen % Mol

N2 0.12

CO2 0.33

CH4 98.77

C2H6 0.53

C3H8 0.23

iC4H10 0.02

nC4H10 0.01

iC5H10 0.00

nC5H10 0.00

C6H14 0.00

TOTAL 100

Komponen % Mol

Nitrogen 0.5

CO2 5

Metana 88

Etana 4

Propana 1.5

i-Butana 0.6

n-Butana 0.4

TOTAL 100

Page 2: Perhitungan Mass Flow.xlsx

300 10080 10020 20

400 30254015

33070

138 km x 28"Pagerungan

TSB

300

m x

28"

80 km x 28"

Santos

7.4

km x

24"

PGN Kalisogo

150

m x

16"

152 km x 28"

10 MMscfd

300 MMscfd 80 MMscfd

20 MMscfd

Page 3: Perhitungan Mass Flow.xlsx

PGN Kalisogo

150

m x

16"

152 km x 28"

PGN Waru

150

m x

16"

26 km x 28"

20 MMscfd 20 MMscfd

PGN G. Sari

150

m x

16"

25 MMscfd

6 km x 28"

PGN Tandes

150

m x

16"

40 MMscfd

11 km x 28"

PGN Gresik

150

m x

16"

9 km x 28"

15 MMscfd

PertagasNiaga

100 MMscfd

150

m x

16"

2.2 km x 24"

PLN Gresik

1.2

km x

24"

PKG

80 MMscfd350 Psig

? MMscfd

4.65 km x 10"

Page 4: Perhitungan Mass Flow.xlsx

KOMPONEN

Komposisi (% Mol)

TSB PAGERUNGAN Mix

CO2 0.08 0.1 0.44 0.12

N2 0.55 0.3 0.54 0.33

CH4 97.69 98.9 97.9 98.77

C2H6 0.87 0.5 0.57 0.53

C3H8 0.47 0.2 0.37 0.23

i-C4H10 0.17 0.1 0.02

n-C4H10 0.12 0.08 0.01

i-C5H12 0.03 0.00

n-C5H12 0.02 0.00

Temperatur (F) 100 100 100Flow (MMscfd) 80 300 20

Pipa Offshore OnshoreDiameter (in) 28 28 24 16Tebal (in) 0.625 0.5 0.5 XS

SANTOS MALEO

Page 5: Perhitungan Mass Flow.xlsx

0.452 0.113 0.0011881.448 0.362 0.003288

394.432 98.608 0.9876992.31 0.5775 0.0052591.05 0.2625 0.002259

0.156 0.039 0.0001590.112 0.028 0.0001180.024 0.006 1.769E-050.016 0.004 1.179E-05400 100

Onshore10Std