AFE Sch-23_24 - Prod Flow Line 3 Inch JNG_2 Sch 40

8/19/2019 AFE Sch-23_24 - Prod Flow Line 3 Inch JNG_2 Sch 40

1/12

P T . P E R T A M I N A E P

K E R J A S A M A O P E R A S I SCHEDULE N

AUTHORIZATION FOR EXPENDITURES - ONSHORE FACILITIES AFE NO.

DATE

OPERATOR : KSO PEP - PD MIAS KOTA !EKASI PRORAM NAME : JATINEARA AS PRODUCTION - FLO" LINES 3# START DATE

CONTRACT AREA : JATINEARA FIELD PROJECT NAME : JATINEARA AS PRODUCTION - FLO" LINES 3# COMPLETION

CONTRACT AREA NO. : PLACED INTO

CLOSE OUT D

DESCRIPTION

RE%ISED !UDET A C T U A L E X P E N D I T U R E S

TOTAL

1 2 3 ) * +

1 CI%IL CONSTRUCTION

2 S/e4

3 E4ee/4 - L5678

) - A9/57

* Ste P/ep7/7t5

+ C5;t/6t5

, S9t5t78

!UILDIN

< E4ee/4 - L567810 - A9/57

11 M7te/78;

12 C5;t/6t5;

13 T/7;p5/t7t5

1) S9t5t78

1* OIL PRODUCTION FACILITIES

1+ E4ee/4

1, M7te/78;

1 I;t7887t5

1< T/7;p5/t7t5

20 S9t5t78

21 AS PRODUCTION FACILITIES

22 E4ee/423 M7te/78;

2) I;t7887t5

2* T/7;p5/t7t5

2+ S9t5t78

2, UTILITIES FACILITIES

2 E4ee/4

2< M7te/78;

30 I;t7887t5

31 T/7;p5/t7t5

32 S9t5t78

33 FLO" LINE 3#

3) E4ee/4 - 21=)3< 3.2))0,+)3

3* M7te/78; 13*=3*+ ),2=0< ,1.*2++2)2

3+ I;t7887t5 2


2/12

P T . P E R T

K E R J A S A M

COMPONENT L

ORIINAL !UDET

UANTIT OTHER COSTS TOTAL COSTS UNIT

1 2 3 ) *

Flow Line Jng-2 To Jng-1 :

1 Ppe= Le= 3# CS= S>8;= R-!= !E= DRL= S6?-)0 1=))0 > 2) 3)=*+0

2 E895= 3# S>8;= L54 R7;=


3/12

T$T$ '$(T)

Uraian

TH. 2011 T

Tri Wulan IV Tri Wulan I Tri

OKT NOP DES JAN FEB MRT APR

Dou!"n T"ni#

Pro#"# S.$%ain

D"li&"r' Ti!"

P"!a#an(an

AFE No. 11)*+02

P"n(a,aan - P"!a#an(an Flo /

!""r4 S5%.304 BE4 S"a!l"##4 DR/ u- JN6)+


4/12

H. 2012

Wulan II Tri Wulan III

MEI JUN JU/ A6T SEP

in" Dia!""r + 3+00

nu Su!ur JN6)14 JN6)2


5/12

ESTIMASI !IAA PENADAAN DAN PEMASANAN PIPA 3#

P774 pp7 )=300

E;t>7; 977&6? 7>& >ete/ p774 30.ete/ pp7 3

T5t78 3


6/12

>ete/

US&6?&>ete/

6?

US

COST ESTIMATE= USD

UANTIT UNIT

2 3 ) *

= DRL ,20 t 2,0 18e;; 20 e7 30 +00

e6 3 e7 100 300

L '12 >( + t 00 )=00

5 3 e7 1=200 3=+00)300 >ete/ 22


7/12

JNG-01

Oil Q Gross Q Cond Q gas Pr

(bopd) (blpd) (blpd) (%) (mscfd) TT T!" TP#

$ &1' 1'& $*'&* 1'1

$ 1+,'+ '&$ $*'&* 1'11 *01'$ '*1 &,' 1'1

1$ *,1' '$ ,+'1$ 1$$'

$ $&+' '$+ &1'+ 1*,'$



1 0 ,+'11 100 1$,0'*1 **'* 10'+1

1$ 0 1*'+* 100 000'*+ +'1 11'$

1, 0 *' 100 1**'* '* 1*'0,



1 1&,,'&$ **',$ $',,

1$ 1+1'0$ 1+&'+$ 1'1

1, 1,,'*1 1&' +*'

J+-02



1$ 1,&'*1 ,,'*&

1 1$,0'& ,,'*&

10 1&+'&0 +*'

$ +'+ +'1

J+-03



Jepi.an(mm)

/a.erCu.

Jepi.an(mm)

/a.erCu.

Jepi.an(mm)

/a.erCu.

Jepi.an

(mm)

/a.er

Cu.

Jepi.an(mm)

/a.er

Cu.


8/12

$ *'* &+'&+ &$',

+ +0 ,1'0* &,'

10 101'*0 0*' *'$1

1 1*'0 +', *,'

1$ 11,'00 1&' $',,

1 110'00 '* *$'++



1$ 1*'00 1,,'0+ 10$'$*

1 1*+0'0 0*' ,,'*&

$ $'* *11', ++'1$

+ ,'$ &**'0& ,'&

10 1$1'*0 $,' ,*'

1 1$1$',0 ,+'$ 10'+

Jepi.an

(mm)

/a.erCu.


9/12

P2G2 *$+ - *1 1-Oc.-+, 1+-Oc.-+,

essure (Psi) #G

T# TC Tsep Oil Gas

*$'++ 100'&

*$'++ ,$'+*$'++ *'

*$'++ +'+

*$'++ +$

P2G2 &,1 - &,* 1,-Oc.-+,

essure (Psi) #G

T# TC Tsep Oil Gas

*'** +$

*'** +,'$

*'** ,$'+

P2G2

&* - &

-Oc.-+,&* - &0

essure (Psi) #G

T# TC Tsep Oil Gas

+'&& +$

+'&& +&'

+'&& +&'

Perfora.ion

Open 3a.e #4u.2n 3a.e

2n.er5al

( m )

6-1&3 *, - *+ 10-7ar-,1

essure (Psi) #G

T# TC Tsep Oil Gas

1' 1'1 +$

,+'$ 1'1 *'

*11', 1'1 $+',

$,', 1'1 $+',

Perfora.ion

Open 3a.e #4u.2n 3a.e

2n.er5al

( m )

6-1&8 &$'* - &$'* -7a9-,& &-7a9-,&

essure (Psi) #G

T# TC Tsep Oil Gas

Temp(o!) Temp (o!) Temp (o!)



Nama"apisan

Temp

(o!) Temp (o!) Temp (o!)

Nama

"apisan



10/12

&'$$ +,'$

&'$$ +,'$

&'$$ +$

&'$$ +$

&'$$ +,'$

&'$$ +'+

6-1& & - && $-7a9-,& +-7a9-,&

essure (Psi) #G

T# TC Tsep Oil Gas

+*' +0'$

+*' +'+

+*' +&'

+*' +0'$

+*' +'+

+*'

Temp

(o!) Temp (o!) Temp (o!)


11/12

Tes.

Tes.

Tes.

No.e

No.e

(oP2)

(oP2)

(oP2)

Tes.

(:"-2)

(oP2)

Tes.(:"-2)

(oP2)


12/12

Tes.(:"-22)

(oP2)

Documents

AFE Sch-23_24 - Prod Flow Line 3 Inch JNG_2 Sch 40