presentation 26 agustus 2015

8/20/2019 Presentation 26 Agustus 2015

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Managing New Feed Gas Entrance

in East Kal Pipeline Network System

Hasanuddin Ritonga (1206230725)

Atan Tuahta (1206227535)


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Outline

Background

East Kalimantan Profile 2!"#22$

East Kalimantan Pipeline System %iagram

&ases

Simulation 'esult

Summary


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Background

(ico as pipeline operator )as responsi*ility to deli+er andmanage gas e,port in East Kalimantan pipeline system-

.)e gas is categori/ed *ased on &01 composition- ean gas is

define as gas e,port w)ic) )a+e relati+ely )ig)er &01 t)an t)e

ot)er gas 3ric) gas4-

ean gas is prioriti/ed to *e deli+ered to domestic industry

w)ic) prefer to recei+e )ig)er &01 gas-

5ntil lean gas can !6 fulfill domestic7 t)e s)ortage of

domestic demand 31" MMscfd4 will *e make up *y ric) gas-

.)e remaining gas will *e deli+ered to Bontang NG .)e Bontang NG )as " trains a+aila*le7 wit) &O2 feed gas

limitation of 86 e,cept for train 0 of 9-" 6-

Some cases of upstream field s)utdown 3and also pipeline

failure4 may cause different feed gas composition in inlet

Bontang NG causing plant operation distur*ance-


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East Kalimantan Profil (2015!2027)

(units in ""s#fd)

Plant 2015 2016 2017 201$ 201% 2020 2021 2022 2023 202& 2025 2026 2027

A1!A6 : !$! 98 2" ! : !

'1 !$ 812 9"$ 1;2 :1: :2: :!8 2!$ ;; ;1 9" "" "

'2 "$2 "9$ 1"" ::! 221 22! !12 "8 ": :; :" :2 2!

'3 !$ ; !1 8 " 1 2

1!3 " 1" 2; !"

$1 ! ! ! ! ;9 ": !; 9

E1!E3 ! ! ! 2 : 9 !! !8 : 1: "" 92 92

*1 "! 8" 8 ": 2! 1

*2+ :;9 122 122 ::; 2!9 !9: !21

*2++ !: !9 !9 !9 !;: 29$ :!; :"$

*3 9! :2" :1! :1! :!! 289 28$ 28$

,+ 18 !11 !11 !11 !11 !:: 9!

,++ 2; 2; 2; 2; 2; 2; 2; 2"$ !8: !:! ;:

Total 22! !$89 !$1$ !18$ !!$2 !2;; !882 !9"8 !192 !2$9 !!$ !1; ;;1

=> gas to 'ic) Pipeline==> gas to ean Pipeline


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G?S &OMPOS@.@ON

P-A.T A1!A6 '1 '2 '3 1 E *1 *2 *3 ,

/2 !!-:! 1-:" 1-$ !1-29 !!-! -$ 8-9 2-9 !-2 !-;9 !-"

.2 -!: -8 -" -" -" -22 -! -!; -9 -!$ -1

H& $8-1 89-2! 89-!2 $:-": 8!-9 ;$-"8 8"-: 88-!" ;9-" 88-$1 ;$-!1

2H6 1-88 :-;9 :-$8 9-21 1-12 -2: :- "-! !-:8 1-; -$$

3H$ :-22 2-;! 2-88 :-2: !-9! -12 !-2 :-: -8! 2-8: -1$

i!&H10 -91 -99 -9: -9$ -1 -!; -: -1; -!9 -19 -!2

n!&H10 -$; -$! -$: -; -:: -22 -: -92 -2: -9 -!"

i!5H12 -2; -:! -: -:2 -!$ -!! -! -!1 -8 -!1 -$

n!5H12 -1! -!; -2 -2! -; -$ !-! -! -9 -! -"

6H1& -1 -92 -92 -"8 -:: -29 - -!! -!1 -!! -!

.o!Pntan - - - - - - - - - - -

#lo!Han -" -: -! -: - -! - - - - -!

'nn -9 -: -! -1 - - - - - -! -

Tolun -: -2 - -2 - - - - - - -

Ethl!'nn - - - - - - - - - - -

"P/!4ln -2 - - - - - - - - - -

? [email protected] @N 6 MO

Rlatil -anr


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East Kalimantan Pipeline System

Badak E,port

Manifold

-an ,as Pilin Ri#h ,as Pilin


7/12

&?SES

as8tud

as 19

.ormalas

as 29

'1 Tri 50:

as 39

'2 Tri

as &9

Tri

as 59

*2 Tri (*3to 8ul

omsti#)

as 69

*3 Tri

as 79

, Tri (*2to 8ulomsti#)

as $9

omsti#Tri 250""8*

.o simulate t)e impact of *ig gas producer 3A! MMscfd4

s)utdown


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2!" 2!9 2!$ 2!8 2!; 22 22! 222 22: 221 22" 229 22$

"

!

!"

2

2"

as &

ean Gas 'ic) Gas

Flow 'ate in Some

&ases

"

!

!"

2

2"

(as 1

'ic) Gas ean Gas

ear

Flow 'ate 3MMS&F%4

"

!

!"

2

2"

(as 5

'ic) Gas ean Gas

ear

Flow 'ate 3MMS&F%4


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2!" 2!9 2!$ 2!8 2!; 22 22! 222 22: 221 22" 229 22$-

!-

2-

:-

1-

"-

9-

$-

8-

;-

&ase! &ase2 &ase: &ase1 &ase" &ase9 &ase$ &ase8

;ar

omosition of /2 (:)

Percentage in eac) gas outlet

2!" 2!9 2!$ 2!8 2!; 22 22! 222 22: 221 22" 229 22$

#!

#-"

-"

!

!-"

2

2-"

:

:-"

1

(/2 )iffrn#s


10/12

S5MM?'

Starting from 227 F2== start to produce lean gas to

fulfill domestic demand

&ase " at 22$ s)ows t)at t)e East Kal gas e,port only

for domestic industry causing Bontang NG s)utdowndue to no gas supply-

?ll cases s)ow t)e impact of upstream plant s)utdown

regards to &O2 composition will not causing Bontang NG

s)utdown-


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'ecomendation

.o c)eck to Bontang NG w)et)er t)e significant

composition c)anges in year 222#22" can affect plant

distur*ance-


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.0?NK O5

presentation 26 agustus 2015

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