2025-02-19T09:02:45+00:00
2025-02-19T09:02:45+00:00
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Company
C
o
m
p
a
n
y
Document
D
o
c
u
m
e
n
t
ID
I
D
11111111100011001
1
1
1
1
1
1
1
1
1
0
0
0
1
1
0
0
1
Sheet
S
h
e
e
t
of
o
f
Sheets
S
h
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e
t
s
1
1
/
/
44
4
4
Validity
V
a
l
i
d
i
t
y
Status
S
t
a
t
u
s
Revision
R
e
v
i
s
i
o
n
Number
N
u
m
b
e
r
AB-DE
A
B
-
D
E
03
0
3
PROJECT
P
R
O
J
E
C
T
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
for
f
o
r
Project
P
r
o
j
e
c
t
AB-DE
A
B
-
D
E
03
0
3
21-09-24
2
1
-
0
9
-
2
4
Issued
I
s
s
u
e
d
for
f
o
r
Information
I
n
f
o
r
m
a
t
i
o
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Project
P
r
o
j
e
c
t
Team
T
e
a
m
M.Schmid
M
.
S
c
h
m
i
d
M.Schmid
M
.
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c
h
m
i
d
AB-DE
A
B
-
D
E
02
0
2
20-11-20
2
0
-
1
1
-
2
0
Issued
I
s
s
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d
for
f
o
r
Information
I
n
f
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m
a
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i
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Project
P
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Team
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.
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M.Schmid
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AB-DE
A
B
-
D
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01
0
1
30-09-20
3
0
-
0
9
-
2
0
Issued
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for
f
o
r
Information
I
n
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Team
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d
AB-DE
A
B
-
D
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00
0
0
17-09-20
1
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9
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2
0
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for
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Information
I
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f
o
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m
a
t
i
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Project
P
r
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j
e
c
t
Team
T
e
a
m
M.Schmid
M
.
S
c
h
m
i
d
M.Schmid
M
.
S
c
h
m
i
d
Validity
V
a
l
i
d
i
t
y
Revision
R
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v
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o
n
Status
S
t
a
t
u
s
Number
N
u
m
b
e
r
Date
D
a
t
e
Description
D
e
s
c
r
i
p
t
i
o
n
Prepared
P
r
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p
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Checked
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d
Approved
A
p
p
r
o
v
e
d
Revision
R
e
v
i
s
i
o
n
Index
I
n
d
e
x
Company
C
o
m
p
a
n
y
logo
l
o
g
o
and
a
n
d
business
b
u
s
i
n
e
s
s
name
n
a
m
e
Company
C
o
m
p
a
n
y
Document
D
o
c
u
m
e
n
t
ID
I
D
11111111100011001
1
1
1
1
1
1
1
1
1
0
0
0
1
1
0
0
1
Document
D
o
c
u
m
e
n
t
ID
I
D
Contractor
C
o
n
t
r
a
c
t
o
r
logo
l
o
g
o
and
a
n
d
business
b
u
s
i
n
e
s
s
name
n
a
m
e
Contractor
C
o
n
t
r
a
c
t
o
r
Document
D
o
c
u
m
e
n
t
ID
I
D
11111111100011001
1
1
1
1
1
1
1
1
1
0
0
0
1
1
0
0
1
Project
P
r
o
j
e
c
t
name
n
a
m
e
PROJECT
P
R
O
J
E
C
T
Document
D
o
c
u
m
e
n
t
Title
T
i
t
l
e
Facility
F
a
c
i
l
i
t
y
and
a
n
d
Sub
S
u
b
Facility
F
a
c
i
l
i
t
y
Name
N
a
m
e
Scale
S
c
a
l
e
n.a.
n
.
a
.
Supersedes
S
u
p
e
r
s
e
d
e
s
N.
N
.
Sheet
S
h
e
e
t
of
o
f
Sheets
S
h
e
e
t
s
1
1
/
/
55
5
5
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
for
f
o
r
Project
P
r
o
j
e
c
t
Superseded
S
u
p
e
r
s
e
d
e
d
by
b
y
N.
N
.
Plant
P
l
a
n
t
Area
A
r
e
a
n.a.
n
.
a
.
Plant
P
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a
n
t
Unit
U
n
i
t
n.a.
n
.
a
.
Software:
S
o
f
t
w
a
r
e
:
Microsoft
M
i
c
r
o
s
o
f
t
Word
W
o
r
d
File
F
i
l
e
Name:
N
a
m
e
:
11111111100011001_CDFDF_54.doc
1
1
1
1
1
1
1
1
1
0
0
0
1
1
0
0
1
_
C
D
F
D
F
_
5
4
.
d
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This
T
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document
d
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is
i
s
property
p
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p
e
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of
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f
DRIMCO.
D
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.
It
I
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shall
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l
neither
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be
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shown
s
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o
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to
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o
Third
T
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d
Parties
P
a
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i
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s
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n
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used
u
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e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
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than
t
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those
t
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for
f
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which
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sent.
s
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.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
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01
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Issued
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for
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Information
I
n
f
o
r
m
a
t
i
o
n
–
–
Flexible
F
l
e
x
i
b
l
e
Jumper
J
u
m
p
e
r
selected
s
e
l
e
c
t
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d
on
o
n
2/4
2
/
4
02
0
2
Issued
I
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u
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for
f
o
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Information
I
n
f
o
r
m
a
t
i
o
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–
–
Update
U
p
d
a
t
e
of
o
f
Design
D
e
s
i
g
n
Data
D
a
t
a
Design
D
e
s
i
g
n
–
–
Section
S
e
c
t
i
o
n
10.1
1
0
.
1
03
0
3
Issued
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for
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Information
I
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–
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U
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granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
INDEX
I
N
D
E
X
1
1
EXECUTIVE
E
X
E
C
U
T
I
V
E
SUMMARY
S
U
M
M
A
R
Y
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5
5
2
2
INTRODUCTION
I
N
T
R
O
D
U
C
T
I
O
N
..................................................................................................................................................
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6
6
2.1
2
.
1
DEVELOPMENT
D
E
V
E
L
O
P
M
E
N
T
..........................................................................................................................................................................................
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6
6
2.2
2
.
2
DEVELOPMENT
D
E
V
E
L
O
P
M
E
N
T
STRATEGY
S
T
R
A
T
E
G
Y
...........................................................................................................................................................................
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6
6
3
3
LOCAL
L
O
C
A
L
ACTS,
A
C
T
S
,
LAWS,
L
A
W
S
,
RULES
R
U
L
E
S
AND
A
N
D
REGULATIONS
R
E
G
U
L
A
T
I
O
N
S
.............................................................................
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7
7
3.1
3
.
1
ENVIRONMENTAL
E
N
V
I
R
O
N
M
E
N
T
A
L
EMISSION
E
M
I
S
S
I
O
N
LIMITS
L
I
M
I
T
S
...............................................................................................................................................................
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7
7
3.2
3
.
2
REGULATORY
R
E
G
U
L
A
T
O
R
Y
COMPLIANCE
C
O
M
P
L
I
A
N
C
E
.........................................................................................................................................................................
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7
7
3.3
3
.
3
ORDER
O
R
D
E
R
OF
O
F
PRECEDENCE
P
R
E
C
E
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E
N
C
E
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7
7
4
4
ABBREVIATIONS,
A
B
B
R
E
V
I
A
T
I
O
N
S
,
REFERENCES,
R
E
F
E
R
E
N
C
E
S
,
CODES
C
O
D
E
S
&
&
STANDARDS
S
T
A
N
D
A
R
D
S
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8
8
4.1
4
.
1
ABBREVIATIONS
A
B
B
R
E
V
I
A
T
I
O
N
S
AND
A
N
D
ACRONYMS
A
C
R
O
N
Y
M
S
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8
8
4.3
4
.
3
DEFINITIONS
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E
F
I
N
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T
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O
N
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10
1
0
4.4
4
.
4
REFERENCE
R
E
F
E
R
E
N
C
E
DOCUMENTS
D
O
C
U
M
E
N
T
S
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10
1
0
4.5
4
.
5
CODES
C
O
D
E
S
&
&
STANDARDS
S
T
A
N
D
A
R
D
S
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11
1
1
4.6
4
.
6
UNITS
U
N
I
T
S
OF
O
F
MEASUREMENTS
M
E
A
S
U
R
E
M
E
N
T
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12
1
2
4.7
4
.
7
COORDINATE
C
O
O
R
D
I
N
A
T
E
GRID
G
R
I
D
REFERENCE
R
E
F
E
R
E
N
C
E
SYSTEM
S
Y
S
T
E
M
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13
1
3
5
5
PROJECT
P
R
O
J
E
C
T
DESCRIPTION
D
E
S
C
R
I
P
T
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O
N
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14
1
4
5.1
5
.
1
DEVELOPMENT
D
E
V
E
L
O
P
M
E
N
T
SCENARIO
S
C
E
N
A
R
I
O
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14
1
4
6
6
GENERAL
G
E
N
E
R
A
L
LOCATION
L
O
C
A
T
I
O
N
DATA
D
A
T
A
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15
1
5
6.1
6
.
1
CLIMATOLOGY
C
L
I
M
A
T
O
L
O
G
Y
AND
A
N
D
METOCEAN
M
E
T
O
C
E
A
N
DATA
D
A
T
A
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15
1
5
6.1.1
6
.
1
.
1
Water
W
a
t
e
r
Depths
D
e
p
t
h
s
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15
1
5
6.1.2
6
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1
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2
Offshore
O
f
f
s
h
o
r
e
Plant
P
l
a
n
t
Location
L
o
c
a
t
i
o
n
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15
1
5
6.1.3
6
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1
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3
Onshore
O
n
s
h
o
r
e
Plant
P
l
a
n
t
Location
L
o
c
a
t
i
o
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5
6.1.4
6
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1
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4
Enviromental
E
n
v
i
r
o
m
e
n
t
a
l
Data
D
a
t
a
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15
1
5
6.2
6
.
2
GEOPHYSICAL
G
E
O
P
H
Y
S
I
C
A
L
AND
A
N
D
GEOTECHNICAL
G
E
O
T
E
C
H
N
I
C
A
L
DATA
D
A
T
A
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16
1
6
6.2.1
6
.
2
.
1
Geotechnical
G
e
o
t
e
c
h
n
i
c
a
l
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16
1
6
6.2.2
6
.
2
.
2
Geophysical
G
e
o
p
h
y
s
i
c
a
l
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16
1
6
6.2.3
6
.
2
.
3
Bathymetry
B
a
t
h
y
m
e
t
r
y
Data
D
a
t
a
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16
1
6
6.2.4
6
.
2
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4
Geohazard
G
e
o
h
a
z
a
r
d
Assessment
A
s
s
e
s
s
m
e
n
t
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17
1
7
6.2.5
6
.
2
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5
Earthquake
E
a
r
t
h
q
u
a
k
e
Data
D
a
t
a
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17
1
7
7
7
RESERVOIR
R
E
S
E
R
V
O
I
R
MANAGEMENT
M
A
N
A
G
E
M
E
N
T
BASIS
B
A
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18
1
8
7.1
7
.
1
MAIN
M
A
I
N
RESERVOIR
R
E
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E
R
V
O
I
R
DATA
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A
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A
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18
1
8
7.2
7
.
2
RESERVOIR
R
E
S
E
R
V
O
I
R
FLUID
F
L
U
I
D
COMPOSITION
C
O
M
P
O
S
I
T
I
O
N
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20
2
0
7.3
7
.
3
PRODUCTION
P
R
O
D
U
C
T
I
O
N
CAPACITY
C
A
P
A
C
I
T
Y
OVERVIEW
O
V
E
R
V
I
E
W
AND
A
N
D
PROFILES
P
R
O
F
I
L
E
S
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21
2
1
8
8
DRILLING
D
R
I
L
L
I
N
G
&
&
COMPLETIONS
C
O
M
P
L
E
T
I
O
N
S
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29
2
9
8.1
8
.
1
DRILLING
D
R
I
L
L
I
N
G
AND
A
N
D
COMPLETIONS
C
O
M
P
L
E
T
I
O
N
S
OVERVIEW
O
V
E
R
V
I
E
W
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29
2
9
8.2
8
.
2
WELLS
W
E
L
L
S
TARGETS
T
A
R
G
E
T
S
COORDINATES
C
O
O
R
D
I
N
A
T
E
S
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29
2
9
8.3
8
.
3
PRELIMINARY
P
R
E
L
I
M
I
N
A
R
Y
CASING
C
A
S
I
N
G
DESIGN
D
E
S
I
G
N
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30
3
0
8.4
8
.
4
COMPLETION
C
O
M
P
L
E
T
I
O
N
SCHEMATICS
S
C
H
E
M
A
T
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C
S
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33
3
3
8.5
8
.
5
PRELIMINARY
P
R
E
L
I
M
I
N
A
R
Y
METALLURGY
M
E
T
A
L
L
U
R
G
Y
AND
A
N
D
ELASTOMERS
E
L
A
S
T
O
M
E
R
S
SELECTION
S
E
L
E
C
T
I
O
N
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35
3
5
9
9
FLUID
F
L
U
I
D
DATA
D
A
T
A
AND
A
N
D
PRODUCTION
P
R
O
D
U
C
T
I
O
N
CHEMISTRY
C
H
E
M
I
S
T
R
Y
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36
3
6
9.1
9
.
1
RESERVOIR
R
E
S
E
R
V
O
I
R
FLUID
F
L
U
I
D
PROPERTIES
P
R
O
P
E
R
T
I
E
S
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36
3
6
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
9.2
9
.
2
RESERVOIR
R
E
S
E
R
V
O
I
R
FLUID
F
L
U
I
D
COMPOSITION
C
O
M
P
O
S
I
T
I
O
N
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36
3
6
9.3
9
.
3
SCALE
S
C
A
L
E
POTENTIAL
P
O
T
E
N
T
I
A
L
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36
3
6
9.4
9
.
4
WAX
W
A
X
FORMATION
F
O
R
M
A
T
I
O
N
AND
A
N
D
RHEOLOGY
R
H
E
O
L
O
G
Y
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36
3
6
9.5
9
.
5
HYDRATE
H
Y
D
R
A
T
E
EQUILIBRIUM
E
Q
U
I
L
I
B
R
I
U
M
CURVES
C
U
R
V
E
S
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36
3
6
9.6
9
.
6
HYDROGEN
H
Y
D
R
O
G
E
N
SULPHIDE
S
U
L
P
H
I
D
E
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37
3
7
9.7
9
.
7
ASPHALTENES
A
S
P
H
A
L
T
E
N
E
S
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37
3
7
9.8
9
.
8
MATERIAL
M
A
T
E
R
I
A
L
SELECTION
S
E
L
E
C
T
I
O
N
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37
3
7
9.8.1
9
.
8
.
1
CO2
C
O
2
Corrosion
C
o
r
r
o
s
i
o
n
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37
3
7
9.9
9
.
9
FLOW
F
L
O
W
ASSURANCE
A
S
S
U
R
A
N
C
E
ISSUES
I
S
S
U
E
S
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38
3
8
9.10
9
.
1
0
FLOWING
F
L
O
W
I
N
G
AND
A
N
D
SHUT
S
H
U
T
IN
I
N
CONDITION
C
O
N
D
I
T
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O
N
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38
3
8
9.10.1
9
.
1
0
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1
Flowing
F
l
o
w
i
n
g
Well
W
e
l
l
Head
H
e
a
d
Pressure
P
r
e
s
s
u
r
e
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38
3
8
9.10.2
9
.
1
0
.
2
Flowing
F
l
o
w
i
n
g
Well
W
e
l
l
Head
H
e
a
d
Temperature
T
e
m
p
e
r
a
t
u
r
e
................................................................................................................
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39
3
9
9.10.3
9
.
1
0
.
3
Topside
T
o
p
s
i
d
e
Arrival
A
r
r
i
v
a
l
Pressure/Temperature
P
r
e
s
s
u
r
e
/
T
e
m
p
e
r
a
t
u
r
e
........................................................................................................
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39
3
9
9.10.3.1
9
.
1
0
.
3
.
1
Operating
O
p
e
r
a
t
i
n
g
Cases
C
a
s
e
s
...............................................................................................................................................
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39
3
9
9.10.3.2
9
.
1
0
.
3
.
2
Inlet
I
n
l
e
t
Flowrate
F
l
o
w
r
a
t
e
FPU
F
P
U
JKK
J
K
K
........................................................................................................................................
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.
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40
4
0
9.10.3.3
9
.
1
0
.
3
.
3
Target
T
a
r
g
e
t
LP
L
P
Max
M
a
x
Flowrate
F
l
o
w
r
a
t
e
.......................................................................................................................................
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41
4
1
9.11
9
.
1
1
PRODUCT
P
R
O
D
U
C
T
SPECIFICATION
S
P
E
C
I
F
I
C
A
T
I
O
N
.........................................................................................................................................................................
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42
4
2
9.11.1
9
.
1
1
.
1
Produced
P
r
o
d
u
c
e
d
Oil
O
i
l
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
............................................................................................................................
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42
4
2
9.11.2
9
.
1
1
.
2
Produced
P
r
o
d
u
c
e
d
Treated
T
r
e
a
t
e
d
Water
W
a
t
e
r
.............................................................................................................................
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42
4
2
9.11.3
9
.
1
1
.
3
H2S
H
2
S
Content
C
o
n
t
e
n
t
................................................................................................................................................
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42
4
2
9.11.4
9
.
1
1
.
4
CO2
C
O
2
Content
C
o
n
t
e
n
t
...............................................................................................................................................
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43
4
3
9.12
9
.
1
2
FIELD
F
I
E
L
D
FLOWRATES
F
L
O
W
R
A
T
E
S
FOR
F
O
R
DESIGN
D
E
S
I
G
N
PURPOSE
P
U
R
P
O
S
E
................................................................................................................................................
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43
4
3
10
1
0
FACILITIES
F
A
C
I
L
I
T
I
E
S
......................................................................................................................................................
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44
4
4
10.1
1
0
.
1
SUBSEA,
S
U
B
S
E
A
,
UMBILICAL
U
M
B
I
L
I
C
A
L
AND
A
N
D
FLOWLINES
F
L
O
W
L
I
N
E
S
..........................................................................................................................................................
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44
4
4
10.1.1
1
0
.
1
.
1
FPU
F
P
U
............................................................................................................................................................
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44
4
4
10.1.2
1
0
.
1
.
2
Design
D
e
s
i
g
n
Life
L
i
f
e
..................................................................................................................................................
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44
4
4
10.1.3
1
0
.
1
.
3
Maximum
M
a
x
i
m
u
m
Water
W
a
t
e
r
Depth
D
e
p
t
h
.............................................................................................................................
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44
4
4
10.1.4
1
0
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1
.
4
Main
M
a
i
n
Subsea
S
u
b
s
e
a
Equipment
E
q
u
i
p
m
e
n
t
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44
4
4
10.1.5
1
0
.
1
.
5
Umbilicals
U
m
b
i
l
i
c
a
l
s
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45
4
5
10.1.6
1
0
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1
.
6
Control
C
o
n
t
r
o
l
System
S
y
s
t
e
m
Description
D
e
s
c
r
i
p
t
i
o
n
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46
4
6
10.1.7
1
0
.
1
.
7
Flowlines
F
l
o
w
l
i
n
e
s
System
S
y
s
t
e
m
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46
4
6
11
1
1
HEALTH,
H
E
A
L
T
H
,
SAFETY,
S
A
F
E
T
Y
,
ENVIRONMENT
E
N
V
I
R
O
N
M
E
N
T
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48
4
8
11.1
1
1
.
1
SAFETY
S
A
F
E
T
Y
CRITERIA
C
R
I
T
E
R
I
A
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48
4
8
11.2
1
1
.
2
HEALTH
H
E
A
L
T
H
CONSIDERATIONS
C
O
N
S
I
D
E
R
A
T
I
O
N
S
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49
4
9
AS
A
S
PER
P
E
R
ABOVE,
A
B
O
V
E
,
THE
T
H
E
HEALTH
H
E
A
L
T
H
RELATED
R
E
L
A
T
E
D
RISK
R
I
S
K
BASED
B
A
S
E
D
APPROACH
A
P
P
R
O
A
C
H
WILL
W
I
L
L
INCLUDE
I
N
C
L
U
D
E
THE
T
H
E
FOLLOWING
F
O
L
L
O
W
I
N
G
OBJECTIVES
O
B
J
E
C
T
I
V
E
S
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49
4
9
11.3
1
1
.
3
SIMOPS
S
I
M
O
P
S
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49
4
9
11.4
1
1
.
4
RISK
R
I
S
K
IDENTIFICATION
I
D
E
N
T
I
F
I
C
A
T
I
O
N
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49
4
9
11.5
1
1
.
5
ENVIRONMENTAL,
E
N
V
I
R
O
N
M
E
N
T
A
L
,
SOCIAL
S
O
C
I
A
L
AND
A
N
D
HEALTH
H
E
A
L
T
H
IMPACT
I
M
P
A
C
T
ASSESSMENT
A
S
S
E
S
S
M
E
N
T
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51
5
1
12
1
2
GHG
G
H
G
EMISSION
E
M
I
S
S
I
O
N
AND
A
N
D
MITIGATION
M
I
T
I
G
A
T
I
O
N
OF
O
F
CLIMATE
C
L
I
M
A
T
E
CHANGE
C
H
A
N
G
E
EFFECTS
E
F
F
E
C
T
S
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52
5
2
12.1
1
2
.
1
WATER
W
A
T
E
R
MANAGEMENT
M
A
N
A
G
E
M
E
N
T
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52
5
2
13
1
3
REGULARITY
R
E
G
U
L
A
R
I
T
Y
AND
A
N
D
OPERATION
O
P
E
R
A
T
I
O
N
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53
5
3
14
1
4
SIMOPS
S
I
M
O
P
S
AND
A
N
D
CONOPS
C
O
N
O
P
S
REQUIREMENTS
R
E
Q
U
I
R
E
M
E
N
T
S
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54
5
4
15
1
5
ATTACHMENTS
A
T
T
A
C
H
M
E
N
T
S
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.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
.
55
5
5
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
1
1
EXECUTIVE
E
X
E
C
U
T
I
V
E
SUMMARY
S
U
M
M
A
R
Y
This
T
h
i
s
document
d
o
c
u
m
e
n
t
defines
d
e
f
i
n
e
s
the
t
h
e
preliminary
p
r
e
l
i
m
i
n
a
r
y
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
for
f
o
r
the
t
h
e
SURF
S
U
R
F
and
a
n
d
the
t
h
e
Flexible
F
l
e
x
i
b
l
e
Line
L
i
n
e
relevant
r
e
l
e
v
a
n
t
to
t
o
Development
D
e
v
e
l
o
p
m
e
n
t
Project.
P
r
o
j
e
c
t
.
The
T
h
e
document
d
o
c
u
m
e
n
t
comprises
c
o
m
p
r
i
s
e
s
reservoir
r
e
s
e
r
v
o
i
r
characteristics,
c
h
a
r
a
c
t
e
r
i
s
t
i
c
s
,
fluid
f
l
u
i
d
properties
p
r
o
p
e
r
t
i
e
s
and
a
n
d
well
w
e
l
l
production
p
r
o
d
u
c
t
i
o
n
data.
d
a
t
a
.
It
I
t
also
a
l
s
o
contains
c
o
n
t
a
i
n
s
the
t
h
e
available
a
v
a
i
l
a
b
l
e
geomorphological
g
e
o
m
o
r
p
h
o
l
o
g
i
c
a
l
and
a
n
d
meteocean
m
e
t
e
o
c
e
a
n
design
d
e
s
i
g
n
data.
d
a
t
a
.
The
T
h
e
document
d
o
c
u
m
e
n
t
also
a
l
s
o
provides
p
r
o
v
i
d
e
s
a
a
description
d
e
s
c
r
i
p
t
i
o
n
of
o
f
the
t
h
e
preliminary
p
r
e
l
i
m
i
n
a
r
y
system
s
y
s
t
e
m
configuration,
c
o
n
f
i
g
u
r
a
t
i
o
n
,
which
w
h
i
c
h
will
w
i
l
l
be
b
e
further
f
u
r
t
h
e
r
developed
d
e
v
e
l
o
p
e
d
by
b
y
the
t
h
e
Tenderers.
T
e
n
d
e
r
e
r
s
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
will
w
i
l
l
be
b
e
enriched
e
n
r
i
c
h
e
d
and
a
n
d
updated
u
p
d
a
t
e
d
as
a
s
necessary
n
e
c
e
s
s
a
r
y
along
a
l
o
n
g
the
t
h
e
project
p
r
o
j
e
c
t
roadmap
r
o
a
d
m
a
p
and
a
n
d
possibly
p
o
s
s
i
b
l
y
at
a
t
the
t
h
e
beginning
b
e
g
i
n
n
i
n
g
of
o
f
each
e
a
c
h
new
n
e
w
Project
P
r
o
j
e
c
t
phase.
p
h
a
s
e
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
2
2
INTRODUCTION
I
N
T
R
O
D
U
C
T
I
O
N
2.1
2
.
1
Development
D
e
v
e
l
o
p
m
e
n
t
The
T
h
e
discovery
d
i
s
c
o
v
e
r
y
is
i
s
located
l
o
c
a
t
e
d
in
i
n
the
t
h
e
REGION
R
E
G
I
O
N
(Op.
(
O
p
.
40%,
4
0
%
,
Pertamina
P
e
r
t
a
m
i
n
a
30%,
3
0
%
,
Neptune
N
e
p
t
u
n
e
30%)
3
0
%
)
operated
o
p
e
r
a
t
e
d
by
b
y
Ltd.,
L
t
d
.
,
within
w
i
t
h
i
n
the
t
h
e
Kutai
K
u
t
a
i
basin,
b
a
s
i
n
,
offshore
o
f
f
s
h
o
r
e
East
E
a
s
t
Kalimantan
K
a
l
i
m
a
n
t
a
n
area
a
r
e
a
in
i
n
Borneo
B
o
r
n
e
o
island
i
s
l
a
n
d
-
-
Indonesia.
I
n
d
o
n
e
s
i
a
.
REGION
R
E
G
I
O
N
was
w
a
s
awarded
a
w
a
r
d
e
d
in
i
n
22
2
2
nd
n
d
August
A
u
g
u
s
t
2019
2
0
1
9
with
w
i
t
h
gross-
g
r
o
s
s
-
split
s
p
l
i
t
REGION
R
E
G
I
O
N
terms,
t
e
r
m
s
,
however
h
o
w
e
v
e
r
the
t
h
e
effective
e
f
f
e
c
t
i
v
e
date
d
a
t
e
is
i
s
26
2
6
th
t
h
January
J
a
n
u
a
r
y
2020.
2
0
2
0
.
Figure
F
i
g
u
r
e
1:
1
:
Location
L
o
c
a
t
i
o
n
Map
M
a
p
-1
-
1
well,
w
e
l
l
,
operated
o
p
e
r
a
t
e
d
by
b
y
Gas
G
a
s
Brand,
B
r
a
n
d
,
was
w
a
s
spud
s
p
u
d
on
o
n
21
2
1
st
s
t
May
M
a
y
2002
2
0
0
2
in
i
n
water
w
a
t
e
r
depth
d
e
p
t
h
of
o
f
-2,436
-
2
,
4
3
6
ft.
f
t
.
The
T
h
e
well
w
e
l
l
reached
r
e
a
c
h
e
d
a
a
TD
T
D
of
o
f
13,441
1
3
,
4
4
1
ftMD
f
t
M
D
(-13,100
(
-
1
3
,
1
0
0
ftTVDSS)
f
t
T
V
D
S
S
)
on
o
n
7
7
th
t
h
June
J
u
n
e
2002.
2
0
0
2
.
The
T
h
e
discovery
d
i
s
c
o
v
e
r
y
was
w
a
s
already
a
l
r
e
a
d
y
successfully
s
u
c
c
e
s
s
f
u
l
l
y
explored
e
x
p
l
o
r
e
d
by
b
y
the
t
h
e
Gendalo-4
G
e
n
d
a
l
o
-
4
operated
o
p
e
r
a
t
e
d
by
b
y
Unocal
U
n
o
c
a
l
in
i
n
2001.
2
0
0
1
.
Both
B
o
t
h
wells
w
e
l
l
s
lie
l
i
e
to
t
o
the
t
h
e
SW
S
W
of
o
f
Gendalo
G
e
n
d
a
l
o
structure
s
t
r
u
c
t
u
r
e
from
f
r
o
m
which
w
h
i
c
h
discovery
d
i
s
c
o
v
e
r
y
is
i
s
separated
s
e
p
a
r
a
t
e
d
by
b
y
a
a
saddle.
s
a
d
d
l
e
.
2.2
2
.
2
Development
D
e
v
e
l
o
p
m
e
n
t
Strategy
S
t
r
a
t
e
g
y
The
T
h
e
development
d
e
v
e
l
o
p
m
e
n
t
concept
c
o
n
c
e
p
t
of
o
f
is
i
s
subsea
s
u
b
s
e
a
tie-in
t
i
e
-
i
n
to
t
o
the
t
h
e
current
c
u
r
r
e
n
t
existing
e
x
i
s
t
i
n
g
Jangkrik
J
a
n
g
k
r
i
k
facilities
f
a
c
i
l
i
t
i
e
s
considering
c
o
n
s
i
d
e
r
i
n
g
the
t
h
e
available
a
v
a
i
l
a
b
l
e
ullage
u
l
l
a
g
e
at
a
t
the
t
h
e
late
l
a
t
e
life
l
i
f
e
of
o
f
Jangkrik
J
a
n
g
k
r
i
k
and
a
n
d
the
t
h
e
location
l
o
c
a
t
i
o
n
in
i
n
vicinity
v
i
c
i
n
i
t
y
of
o
f
Jangkrik
J
a
n
g
k
r
i
k
Main
M
a
i
n
Clusters.
C
l
u
s
t
e
r
s
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
3
3
LOCAL
L
O
C
A
L
ACTS,
A
C
T
S
,
LAWS,
L
A
W
S
,
RULES
R
U
L
E
S
AND
A
N
D
REGULATIONS
R
E
G
U
L
A
T
I
O
N
S
3.1
3
.
1
Environmental
E
n
v
i
r
o
n
m
e
n
t
a
l
Emission
E
m
i
s
s
i
o
n
Limits
L
i
m
i
t
s
Refer
R
e
f
e
r
to
t
o
[7].
[
7
]
.
Should
S
h
o
u
l
d
some
s
o
m
e
special
s
p
e
c
i
a
l
operations
o
p
e
r
a
t
i
o
n
s
related
r
e
l
a
t
e
d
to
t
o
field
f
i
e
l
d
(e.g.
(
e
.
g
.
pre-commissioning
p
r
e
-
c
o
m
m
i
s
s
i
o
n
i
n
g
activities
a
c
t
i
v
i
t
i
e
s
of
o
f
flowline)
f
l
o
w
l
i
n
e
)
imply
i
m
p
l
y
a
a
possible
p
o
s
s
i
b
l
e
impact
i
m
p
a
c
t
to
t
o
the
t
h
e
environment,
e
n
v
i
r
o
n
m
e
n
t
,
these
t
h
e
s
e
will
w
i
l
l
have
h
a
v
e
to
t
o
be
b
e
properly
p
r
o
p
e
r
l
y
assessed
a
s
s
e
s
s
e
d
with
w
i
t
h
the
t
h
e
HSE
H
S
E
function
f
u
n
c
t
i
o
n
to
t
o
verify
v
e
r
i
f
y
any
a
n
y
constraints
c
o
n
s
t
r
a
i
n
t
s
to
t
o
be
b
e
satisfied.
s
a
t
i
s
f
i
e
d
.
3.2
3
.
2
Regulatory
R
e
g
u
l
a
t
o
r
y
Compliance
C
o
m
p
l
i
a
n
c
e
Refer
R
e
f
e
r
to
t
o
[3]Errore.
[
3
]
E
r
r
o
r
e
.
L'origine
L
'
o
r
i
g
i
n
e
riferimento
r
i
f
e
r
i
m
e
n
t
o
non
n
o
n
è
è
stata
s
t
a
t
a
trovata..
t
r
o
v
a
t
a
.
.
3.3
3
.
3
Order
O
r
d
e
r
of
o
f
Precedence
P
r
e
c
e
d
e
n
c
e
The
T
h
e
local
l
o
c
a
l
acts,
a
c
t
s
,
laws,
l
a
w
s
,
rules
r
u
l
e
s
and
a
n
d
regulations
r
e
g
u
l
a
t
i
o
n
s
applicable
a
p
p
l
i
c
a
b
l
e
to
t
o
this
t
h
i
s
project
p
r
o
j
e
c
t
shall
s
h
a
l
l
be
b
e
the
t
h
e
same
s
a
m
e
of
o
f
those
t
h
o
s
e
relevant
r
e
l
e
v
a
n
t
to
t
o
Jangkrik
J
a
n
g
k
r
i
k
field.
f
i
e
l
d
.
The
T
h
e
most
m
o
s
t
stringent
s
t
r
i
n
g
e
n
t
rules
r
u
l
e
s
shall
s
h
a
l
l
be
b
e
applied.
a
p
p
l
i
e
d
.
In
I
n
the
t
h
e
event
e
v
e
n
t
of
o
f
scope
s
c
o
p
e
overlapping
o
v
e
r
l
a
p
p
i
n
g
of
o
f
different
d
i
f
f
e
r
e
n
t
rules,
r
u
l
e
s
,
the
t
h
e
most
m
o
s
t
stringent
s
t
r
i
n
g
e
n
t
requirement
r
e
q
u
i
r
e
m
e
n
t
shall
s
h
a
l
l
apply.
a
p
p
l
y
.
The
T
h
e
following
f
o
l
l
o
w
i
n
g
shall
s
h
a
l
l
be
b
e
the
t
h
e
order
o
r
d
e
r
of
o
f
precedence,
p
r
e
c
e
d
e
n
c
e
,
1
1
being
b
e
i
n
g
the
t
h
e
highest
h
i
g
h
e
s
t
precedence
p
r
e
c
e
d
e
n
c
e
level
l
e
v
e
l
(see
(
s
e
e
ref.
r
e
f
.
[3]
[
3
]
for
f
o
r
complete
c
o
m
p
l
e
t
e
list
l
i
s
t
of
o
f
applicable
a
p
p
l
i
c
a
b
l
e
standards):
s
t
a
n
d
a
r
d
s
)
:
-
Indonesian
I
n
d
o
n
e
s
i
a
n
Laws,
L
a
w
s
,
Regulations
R
e
g
u
l
a
t
i
o
n
s
and
a
n
d
International
I
n
t
e
r
n
a
t
i
o
n
a
l
Conventions
C
o
n
v
e
n
t
i
o
n
s
signed
s
i
g
n
e
d
and/or
a
n
d
/
o
r
endorsed
e
n
d
o
r
s
e
d
by
b
y
Indonesia,
I
n
d
o
n
e
s
i
a
,
applicable
a
p
p
l
i
c
a
b
l
e
to
t
o
offshore
o
f
f
s
h
o
r
e
installations.
i
n
s
t
a
l
l
a
t
i
o
n
s
.
-
Classification
C
l
a
s
s
i
f
i
c
a
t
i
o
n
Rules
R
u
l
e
s
(as
(
a
s
applicable
a
p
p
l
i
c
a
b
l
e
to
t
o
the
t
h
e
concerned
c
o
n
c
e
r
n
e
d
type
t
y
p
e
of
o
f
equipment),
e
q
u
i
p
m
e
n
t
)
,
Flag
F
l
a
g
Regulations,
R
e
g
u
l
a
t
i
o
n
s
,
Marine
M
a
r
i
n
e
International
I
n
t
e
r
n
a
t
i
o
n
a
l
Rules
R
u
l
e
s
and
a
n
d
Certification
C
e
r
t
i
f
i
c
a
t
i
o
n
Society.
S
o
c
i
e
t
y
.
-
Project
P
r
o
j
e
c
t
Documentation
D
o
c
u
m
e
n
t
a
t
i
o
n
(Appendix
(
A
p
p
e
n
d
i
x
D)
D
)
-
Company
C
o
m
p
a
n
y
Standards
S
t
a
n
d
a
r
d
s
(for
(
f
o
r
new
n
e
w
equipment,
e
q
u
i
p
m
e
n
t
,
last
l
a
s
t
revision
r
e
v
i
s
i
o
n
of
o
f
Company
C
o
m
p
a
n
y
Standards
S
t
a
n
d
a
r
d
s
shall
s
h
a
l
l
be
b
e
used
u
s
e
d
–
–
as
a
s
per
p
e
r
ref.
r
e
f
.
[3]Errore.
[
3
]
E
r
r
o
r
e
.
L'origine
L
'
o
r
i
g
i
n
e
riferimento
r
i
f
e
r
i
m
e
n
t
o
non
n
o
n
è
è
stata
s
t
a
t
a
trovata.).
t
r
o
v
a
t
a
.
)
.
-
International
I
n
t
e
r
n
a
t
i
o
n
a
l
codes
c
o
d
e
s
and
a
n
d
standards.
s
t
a
n
d
a
r
d
s
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
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4
4
ABBREVIATIONS,
A
B
B
R
E
V
I
A
T
I
O
N
S
,
REFERENCES,
R
E
F
E
R
E
N
C
E
S
,
CODES
C
O
D
E
S
&
&
STANDARDS
S
T
A
N
D
A
R
D
S
4.1
4
.
1
Abbreviations
A
b
b
r
e
v
i
a
t
i
o
n
s
and
a
n
d
Acronyms
A
c
r
o
n
y
m
s
The
T
h
e
followings
f
o
l
l
o
w
i
n
g
s
will
w
i
l
l
be
b
e
applied
a
p
p
l
i
e
d
to
t
o
this
t
h
i
s
document:
d
o
c
u
m
e
n
t
:
API
A
P
I
Degree(s)
D
e
g
r
e
e
(
s
)
API
A
P
I
BOPD
B
O
P
D
Barrels
B
a
r
r
e
l
s
of
o
f
Oil
O
i
l
Per
P
e
r
Day
D
a
y
BLPD
B
L
P
D
Barrels
B
a
r
r
e
l
s
of
o
f
Liquid
L
i
q
u
i
d
Per
P
e
r
Day
D
a
y
BWPD
B
W
P
D
Barrels
B
a
r
r
e
l
s
of
o
f
Water
W
a
t
e
r
Per
P
e
r
Day
D
a
y
CDT
C
D
T
Cool
C
o
o
l
Down
D
o
w
n
Time
T
i
m
e
CPT
C
P
T
Cone
C
o
n
e
Penetration
P
e
n
e
t
r
a
t
i
o
n
Test
T
e
s
t
CGR
C
G
R
Condensate
C
o
n
d
e
n
s
a
t
e
Gas
G
a
s
Ratio
R
a
t
i
o
CITV
C
I
T
V
Chemical
C
h
e
m
i
c
a
l
Injection
I
n
j
e
c
t
i
o
n
Throttling
T
h
r
o
t
t
l
i
n
g
Valve
V
a
l
v
e
CJB
C
J
B
Cable
C
a
b
l
e
Jointing
J
o
i
n
t
i
n
g
Box
B
o
x
E&I
E
&
I
Electrical
E
l
e
c
t
r
i
c
a
l
and
a
n
d
Instrumentation
I
n
s
t
r
u
m
e
n
t
a
t
i
o
n
EJB
E
J
B
Electrical
E
l
e
c
t
r
i
c
a
l
Junction
J
u
n
c
t
i
o
n
Box
B
o
x
EPU
E
P
U
Electric
E
l
e
c
t
r
i
c
Power
P
o
w
e
r
Unit
U
n
i
t
FPU
F
P
U
Floating
F
l
o
a
t
i
n
g
Production
P
r
o
d
u
c
t
i
o
n
Unit
U
n
i
t
FTHP
F
T
H
P
Flowing
F
l
o
w
i
n
g
Tubing
T
u
b
i
n
g
Head
H
e
a
d
Pressure
P
r
e
s
s
u
r
e
HC
H
C
Hydrocarbon
H
y
d
r
o
c
a
r
b
o
n
HIPPS
H
I
P
P
S
High
H
i
g
h
Integrity
I
n
t
e
g
r
i
t
y
Pressure
P
r
e
s
s
u
r
e
Protection
P
r
o
t
e
c
t
i
o
n
System
S
y
s
t
e
m
HP
H
P
High
H
i
g
h
Pressure
P
r
e
s
s
u
r
e
HPU
H
P
U
Hydraulic
H
y
d
r
a
u
l
i
c
Power
P
o
w
e
r
Unit
U
n
i
t
ID
I
D
Internal
I
n
t
e
r
n
a
l
Diameter
D
i
a
m
e
t
e
r
ILT
I
L
T
In
I
n
Line
L
i
n
e
Tee
T
e
e
ITT
I
T
T
Invitation
I
n
v
i
t
a
t
i
o
n
To
T
o
Tender
T
e
n
d
e
r
JKK
J
K
K
Jangkrik
J
a
n
g
k
r
i
k
Main
M
a
i
n
JNE
J
N
E
Jangkrik
J
a
n
g
k
r
i
k
North
N
o
r
t
h
East
E
a
s
t
LCP
L
C
P
Local
L
o
c
a
l
Control
C
o
n
t
r
o
l
Panel
P
a
n
e
l
LER
L
E
R
Local
L
o
c
a
l
Equipment
E
q
u
i
p
m
e
n
t
Room
R
o
o
m
LNG
L
N
G
Liquefied
L
i
q
u
e
f
i
e
d
Natural
N
a
t
u
r
a
l
Gas
G
a
s
LP
L
P
Low
L
o
w
Pressure
P
r
e
s
s
u
r
e
MEG
M
E
G
MonoEthylen
M
o
n
o
E
t
h
y
l
e
n
Glycol
G
l
y
c
o
l
MeOH
M
e
O
H
Methanol
M
e
t
h
a
n
o
l
MMBLPD
M
M
B
L
P
D
Million
M
i
l
l
i
o
n
Barrel
B
a
r
r
e
l
of
o
f
liquid
l
i
q
u
i
d
per
p
e
r
day
d
a
y
MMSCFD
M
M
S
C
F
D
Million
M
i
l
l
i
o
n
of
o
f
Standard
S
t
a
n
d
a
r
d
Cubic
C
u
b
i
c
Feets
F
e
e
t
s
per
p
e
r
Day
D
a
y
MSL
M
S
L
Mean
M
e
a
n
Sea
S
e
a
Level
L
e
v
e
l
MWA
M
W
A
Mid
M
i
d
Water
W
a
t
e
r
Arch
A
r
c
h
ND
N
D
Nominal
N
o
m
i
n
a
l
Diameter
D
i
a
m
e
t
e
r
OD
O
D
Outer
O
u
t
e
r
Diameter
D
i
a
m
e
t
e
r
OJB
O
J
B
Optical
O
p
t
i
c
a
l
Junction
J
u
n
c
t
i
o
n
Box
B
o
x
ORF
O
R
F
Onshore
O
n
s
h
o
r
e
Receiving
R
e
c
e
i
v
i
n
g
Facilities
F
a
c
i
l
i
t
i
e
s
P&ID
P
&
I
D
Piping
P
i
p
i
n
g
and
a
n
d
Instrumentation
I
n
s
t
r
u
m
e
n
t
a
t
i
o
n
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
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PLET
P
L
E
T
Pipe
P
i
p
e
Line
L
i
n
e
End
E
n
d
Termination
T
e
r
m
i
n
a
t
i
o
n
PLR
P
L
R
Pig
P
i
g
Laucher
L
a
u
c
h
e
r
Receiver
R
e
c
e
i
v
e
r
ppmv
p
p
m
v
Parts
P
a
r
t
s
per
p
e
r
Million,
M
i
l
l
i
o
n
,
Volumetric
V
o
l
u
m
e
t
r
i
c
PVT
P
V
T
Pressure,
P
r
e
s
s
u
r
e
,
Volume,
V
o
l
u
m
e
,
Temperature
T
e
m
p
e
r
a
t
u
r
e
PW
P
W
Produced
P
r
o
d
u
c
e
d
Water
W
a
t
e
r
RAM
R
A
M
Reliability
R
e
l
i
a
b
i
l
i
t
y
Availability
A
v
a
i
l
a
b
i
l
i
t
y
Maintainability
M
a
i
n
t
a
i
n
a
b
i
l
i
t
y
ROV
R
O
V
Remotely
R
e
m
o
t
e
l
y
Operated
O
p
e
r
a
t
e
d
Vehicle
V
e
h
i
c
l
e
RVP
R
V
P
Reid
R
e
i
d
Vapor
V
a
p
o
r
Pressure
P
r
e
s
s
u
r
e
SCM
S
C
M
Subsea
S
u
b
s
e
a
Control
C
o
n
t
r
o
l
Module
M
o
d
u
l
e
SDU
S
D
U
Subsea
S
u
b
s
e
a
Distribution
D
i
s
t
r
i
b
u
t
i
o
n
Unit
U
n
i
t
SDV
S
D
V
Shut
S
h
u
t
Down
D
o
w
n
Valve
V
a
l
v
e
SoW
S
o
W
Scope
S
c
o
p
e
of
o
f
Work
W
o
r
k
SI
S
I
International
I
n
t
e
r
n
a
t
i
o
n
a
l
System
S
y
s
t
e
m
of
o
f
Units
U
n
i
t
s
SITHP
S
I
T
H
P
Shut-In
S
h
u
t
-
I
n
Tubing
T
u
b
i
n
g
Head
H
e
a
d
Pressure
P
r
e
s
s
u
r
e
SMLS
S
M
L
S
Seamless
S
e
a
m
l
e
s
s
SPS
S
P
S
Subsea
S
u
b
s
e
a
Production
P
r
o
d
u
c
t
i
o
n
System
S
y
s
t
e
m
SURF
S
U
R
F
Subsea,
S
u
b
s
e
a
,
Umbilical,
U
m
b
i
l
i
c
a
l
,
Riser
R
i
s
e
r
and
a
n
d
Flowline
F
l
o
w
l
i
n
e
SSIV
S
S
I
V
Subsea
S
u
b
s
e
a
Safety
S
a
f
e
t
y
Isolation
I
s
o
l
a
t
i
o
n
Valve
V
a
l
v
e
TBD
T
B
D
To
T
o
be
b
e
Defined
D
e
f
i
n
e
d
TUTU
T
U
T
U
Topside
T
o
p
s
i
d
e
Umbilical
U
m
b
i
l
i
c
a
l
Termination
T
e
r
m
i
n
a
t
i
o
n
Unit
U
n
i
t
TVDSS
T
V
D
S
S
True
T
r
u
e
Vertical
V
e
r
t
i
c
a
l
Depth
D
e
p
t
h
SubSea
S
u
b
S
e
a
TVP
T
V
P
True
T
r
u
e
Vapor
V
a
p
o
r
Pressure
P
r
e
s
s
u
r
e
UPS
U
P
S
Uninterruptible
U
n
i
n
t
e
r
r
u
p
t
i
b
l
e
Power
P
o
w
e
r
Supply
S
u
p
p
l
y
UTA
U
T
A
Umbilical
U
m
b
i
l
i
c
a
l
Termination
T
e
r
m
i
n
a
t
i
o
n
Unit
U
n
i
t
XT
X
T
Christmas
C
h
r
i
s
t
m
a
s
Tree
T
r
e
e
WD
W
D
Water
W
a
t
e
r
Depth
D
e
p
t
h
WHFP
W
H
F
P
Well
W
e
l
l
Head
H
e
a
d
Flowing
F
l
o
w
i
n
g
Pressure
P
r
e
s
s
u
r
e
WHSIP
W
H
S
I
P
Well
W
e
l
l
Head
H
e
a
d
Shut-In
S
h
u
t
-
I
n
Pressure
P
r
e
s
s
u
r
e
WHFT
W
H
F
T
Well
W
e
l
l
Head
H
e
a
d
Flowing
F
l
o
w
i
n
g
Temperature
T
e
m
p
e
r
a
t
u
r
e
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
4.3
4
.
3
Definitions
D
e
f
i
n
i
t
i
o
n
s
The
T
h
e
following
f
o
l
l
o
w
i
n
g
definitions
d
e
f
i
n
i
t
i
o
n
s
apply
a
p
p
l
y
to
t
o
this
t
h
i
s
document:
d
o
c
u
m
e
n
t
:
FLOWLINE
F
L
O
W
L
I
N
E
PIPELINE
P
I
P
E
L
I
N
E
SEALINE
S
E
A
L
I
N
E
STABILISED
S
T
A
B
I
L
I
S
E
D
CONDENSATES
C
O
N
D
E
N
S
A
T
E
S
Generic
G
e
n
e
r
i
c
term
t
e
r
m
adopted
a
d
o
p
t
e
d
for
f
o
r
hydrocarbon
h
y
d
r
o
c
a
r
b
o
n
transportation
t
r
a
n
s
p
o
r
t
a
t
i
o
n
lines
l
i
n
e
s
that
t
h
a
t
connect
c
o
n
n
e
c
t
onshore/offshore
o
n
s
h
o
r
e
/
o
f
f
s
h
o
r
e
installations
i
n
s
t
a
l
l
a
t
i
o
n
s
(synonym
(
s
y
n
o
n
y
m
of
o
f
pipeline)
p
i
p
e
l
i
n
e
)
Generic
G
e
n
e
r
i
c
term
t
e
r
m
adopted
a
d
o
p
t
e
d
for
f
o
r
hydrocarbon
h
y
d
r
o
c
a
r
b
o
n
transportation
t
r
a
n
s
p
o
r
t
a
t
i
o
n
lines
l
i
n
e
s
that
t
h
a
t
connect
c
o
n
n
e
c
t
onshore/offshore
o
n
s
h
o
r
e
/
o
f
f
s
h
o
r
e
installations
i
n
s
t
a
l
l
a
t
i
o
n
s
(synonym
(
s
y
n
o
n
y
m
of
o
f
flowline)
f
l
o
w
l
i
n
e
)
Term
T
e
r
m
referred
r
e
f
e
r
r
e
d
to
t
o
hydrocarbon
h
y
d
r
o
c
a
r
b
o
n
transportation
t
r
a
n
s
p
o
r
t
a
t
i
o
n
lines
l
i
n
e
s
that
t
h
a
t
connect
c
o
n
n
e
c
t
offshore
o
f
f
s
h
o
r
e
installations
i
n
s
t
a
l
l
a
t
i
o
n
s
to
t
o
shore
s
h
o
r
e
Treated
T
r
e
a
t
e
d
HC
H
C
Fluid
F
l
u
i
d
that
t
h
a
t
can
c
a
n
be
b
e
stored
s
t
o
r
e
d
at
a
t
ambient
a
m
b
i
e
n
t
temperature
t
e
m
p
e
r
a
t
u
r
e
and
a
n
d
pressure
p
r
e
s
s
u
r
e
in
i
n
liquid
l
i
q
u
i
d
phase
p
h
a
s
e
without
w
i
t
h
o
u
t
significant
s
i
g
n
i
f
i
c
a
n
t
boil-off
b
o
i
l
-
o
f
f
generation.
g
e
n
e
r
a
t
i
o
n
.
4.4
4
.
4
Reference
R
e
f
e
r
e
n
c
e
Documents
D
o
c
u
m
e
n
t
s
[Ref
[
R
e
f
n°]
n
°
]
Document
D
o
c
u
m
e
n
t
Name
N
a
m
e
Document
D
o
c
u
m
e
n
t
Number
N
u
m
b
e
r
Notes
N
o
t
e
s
-
Field
F
i
e
l
d
General
G
e
n
e
r
a
l
Layout
L
a
y
o
u
t
and
a
n
d
Details
D
e
t
a
i
l
s
220814BGDP00039
2
2
0
8
1
4
B
G
D
P
0
0
0
3
9
-
Subsea
S
u
b
s
e
a
Block
B
l
o
c
k
Diagram
D
i
a
g
r
a
m
220814BGRB00036
2
2
0
8
1
4
B
G
R
B
0
0
0
3
6
-
International
I
n
t
e
r
n
a
t
i
o
n
a
l
Codes
C
o
d
e
s
and
a
n
d
Company
C
o
m
p
a
n
y
Standards
S
t
a
n
d
a
r
d
s
220814BGES00006
2
2
0
8
1
4
B
G
E
S
0
0
0
0
6
-
Deleted
D
e
l
e
t
e
d
Deleted
D
e
l
e
t
e
d
-
Field
F
i
e
l
d
Development
D
e
v
e
l
o
p
m
e
n
t
-
-
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
-
Health,
H
e
a
l
t
h
,
Safety
S
a
f
e
t
y
and
a
n
d
Environmental
E
n
v
i
r
o
n
m
e
n
t
a
l
(HSE)
(
H
S
E
)
Philosophy
P
h
i
l
o
s
o
p
h
y
-
Indonesian
I
n
d
o
n
e
s
i
a
n
Environmental
E
n
v
i
r
o
n
m
e
n
t
a
l
Emission
E
m
i
s
s
i
o
n
Limits
L
i
m
i
t
s
-
Development
D
e
v
e
l
o
p
m
e
n
t
–
–
Process
P
r
o
c
e
s
s
Report
R
e
p
o
r
t
220814FGRB00011
2
2
0
8
1
4
F
G
R
B
0
0
0
1
1
000589_DV_CS.HSE.0048.000_01
0
0
0
5
8
9
_
D
V
_
C
S
.
H
S
E
.
0
0
4
8
.
0
0
0
_
0
1
000589_DV_CS.HSE.0118.000_00
0
0
0
5
8
9
_
D
V
_
C
S
.
H
S
E
.
0
1
1
8
.
0
0
0
_
0
0
220814FPRA00013
2
2
0
8
1
4
F
P
R
A
0
0
0
1
3
-
Facilities
F
a
c
i
l
i
t
i
e
s
Report
R
e
p
o
r
t
220814FGRV00012
2
2
0
8
1
4
F
G
R
V
0
0
0
1
2
-
e-EHXT
e
-
E
H
X
T
P&ID
P
&
I
D
220814BUFM00053
2
2
0
8
1
4
B
U
F
M
0
0
0
5
3
-
Control
C
o
n
t
r
o
l
System
S
y
s
t
e
m
Block
B
l
o
c
k
Diagram
D
i
a
g
r
a
m
220814BGFB00037
2
2
0
8
1
4
B
G
F
B
0
0
0
3
7
-
UTA
U
T
A
P&ID
P
&
I
D
220814BUFM00052
2
2
0
8
1
4
B
U
F
M
0
0
0
5
2
-
HIPPS
H
I
P
P
S
P&ID
P
&
I
D
220814BUFM00047
2
2
0
8
1
4
B
U
F
M
0
0
0
4
7
-
Subsea
S
u
b
s
e
a
Structure
S
t
r
u
c
t
u
r
e
P&ID
P
&
I
D
220814BUFM00045
2
2
0
8
1
4
B
U
F
M
0
0
0
4
5
-
TEE
T
E
E
Structure
S
t
r
u
c
t
u
r
e
P&ID
P
&
I
D
220814BUFM00046
2
2
0
8
1
4
B
U
F
M
0
0
0
4
6
-
Corrosion
C
o
r
r
o
s
i
o
n
Control
C
o
n
t
r
o
l
and
a
n
d
Material
M
a
t
e
r
i
a
l
Selection
S
e
l
e
c
t
i
o
n
report
r
e
p
o
r
t
220814BXRV00026
2
2
0
8
1
4
B
X
R
V
0
0
0
2
6
-
Flow
F
l
o
w
Assurance
A
s
s
u
r
a
n
c
e
Report
R
e
p
o
r
t
220814BBRV00014
2
2
0
8
1
4
B
B
R
V
0
0
0
1
4
-
PROJECT
P
R
O
J
E
C
T
field
f
i
e
l
d
development
d
e
v
e
l
o
p
m
e
n
t
drilling
d
r
i
l
l
i
n
g
&
&
COMPLETION
C
O
M
P
L
E
T
I
O
N
PRE-
P
R
E
-
FEASIBILITY
F
E
A
S
I
B
I
L
I
T
Y
STUDY
S
T
U
D
Y
COAP/SU–P-1-P-28155
C
O
A
P
/
S
U
–
P
-
1
-
P
-
2
8
1
5
5
Feasibility
F
e
a
s
i
b
i
l
i
t
y
document
d
o
c
u
m
e
n
t
Feasibility
F
e
a
s
i
b
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l
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y
document
d
o
c
u
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e
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Feasibility
F
e
a
s
i
b
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document
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Feasibility
F
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document
d
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Feasibility
F
e
a
s
i
b
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y
document
d
o
c
u
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e
n
t
Pre-
P
r
e
-
feasibility
f
e
a
s
i
b
i
l
i
t
y
study
s
t
u
d
y
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
-
Pre-FEED
P
r
e
-
F
E
E
D
Work
W
o
r
k
for
f
o
r
IDD
I
D
D
Concept
C
o
n
c
e
p
t
GLO-D200-UFA-BOD-WPI-000-
G
L
O
-
D
2
0
0
-
U
F
A
-
B
O
D
-
W
P
I
-
0
0
0
-
Evaluation
E
v
a
l
u
a
t
i
o
n
10001
1
0
0
0
1
[20]
[
2
0
]
Flow
F
l
o
w
Assurance
A
s
s
u
r
a
n
c
e
Design
D
e
s
i
g
n
Basis
B
a
s
i
s
GLO-D200-UFA-BOD-WPI-000-
G
L
O
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D
2
0
0
-
U
F
A
-
B
O
D
-
W
P
I
-
0
0
0
-
10001
1
0
0
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1
[21]
[
2
1
]
Flow
F
l
o
w
Assurance
A
s
s
u
r
a
n
c
e
Report
R
e
p
o
r
t
220814FPRV00014
2
2
0
8
1
4
F
P
R
V
0
0
0
1
4
[22]
[
2
2
]
Topside
T
o
p
s
i
d
e
Process
P
r
o
c
e
s
s
Description
D
e
s
c
r
i
p
t
i
o
n
220801DPRV10009
2
2
0
8
0
1
D
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R
V
1
0
0
0
9
[23]
[
2
3
]
Phase
P
h
a
s
e
2
2
–
–
Process
P
r
o
c
e
s
s
Verification
V
e
r
i
f
i
c
a
t
i
o
n
Report
R
e
p
o
r
t
–
–
Dual
D
u
a
l
Mode
M
o
d
e
Case
C
a
s
e
750
7
5
0
Inlet
I
n
l
e
t
[24]
[
2
4
]
Jangkrik
J
a
n
g
k
r
i
k
Phase
P
h
a
s
e
2
2
–
–
FEED
F
E
E
D
Process
P
r
o
c
e
s
s
Report
R
e
p
o
r
t
220801BPR00329
2
2
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1
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P
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0
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2
9
220801BGRV00151
2
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0
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1
[25]
[
2
5
]
SPS
S
P
S
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
RP_A11111v1
R
P
_
A
1
1
1
1
1
v
1
–
–
Main
M
a
i
n
(Feb
(
F
e
b
2012)
2
0
1
2
)
[26]
[
2
6
]
EPCI
E
P
C
I
2
2
–
–
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
220802BGRB45230
2
2
0
8
0
2
B
G
R
B
4
5
2
3
0
[27]
[
2
7
]
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
and
a
n
d
Functional
F
u
n
c
t
i
o
n
a
l
Requirements
R
e
q
u
i
r
e
m
e
n
t
s
for
f
o
r
FPU
F
P
U
detail
d
e
t
a
i
l
design
d
e
s
i
g
n
220801DGSH45183
2
2
0
8
0
1
D
G
S
H
4
5
1
8
3
[28]
[
2
8
]
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
for
f
o
r
Merakes
M
e
r
a
k
e
s
Project
P
r
o
j
e
c
t
220800BGRBM1366
2
2
0
8
0
0
B
G
R
B
M
1
3
6
6
[29]
[
2
9
]
Subsea
S
u
b
s
e
a
System
S
y
s
t
e
m
and
a
n
d
Subsea
S
u
b
s
e
a
Control
C
o
n
t
r
o
l
System
S
y
s
t
e
m
Description
D
e
s
c
r
i
p
t
i
o
n
and
a
n
d
philosophy
p
h
i
l
o
s
o
p
h
y
[30]
[
3
0
]
SCS
S
C
S
(Subsea
(
S
u
b
s
e
a
Control
C
o
n
t
r
o
l
System)
S
y
s
t
e
m
)
Data
D
a
t
a
Sheet
S
h
e
e
t
220814BURB00041
2
2
0
8
1
4
B
U
R
B
0
0
0
4
1
220814BUGA00056
2
2
0
8
1
4
B
U
G
A
0
0
0
5
6
[31]
[
3
1
]
Umbilical
U
m
b
i
l
i
c
a
l
System
S
y
s
t
e
m
Data
D
a
t
a
Sheet
S
h
e
e
t
220814BUGA00057
2
2
0
8
1
4
B
U
G
A
0
0
0
5
7
[32]
[
3
2
]
SURF
S
U
R
F
Design
D
e
s
i
g
n
pressure
p
r
e
s
s
u
r
e
definition
d
e
f
i
n
i
t
i
o
n
and
a
n
d
verification
v
e
r
i
f
i
c
a
t
i
o
n
220814BUCA00040
2
2
0
8
1
4
B
U
C
A
0
0
0
4
0
Feasibility
F
e
a
s
i
b
i
l
i
t
y
document
d
o
c
u
m
e
n
t
The
T
h
e
original
o
r
i
g
i
n
a
l
engineering
e
n
g
i
n
e
e
r
i
n
g
design
d
e
s
i
g
n
documentation
d
o
c
u
m
e
n
t
a
t
i
o
n
relevant
r
e
l
e
v
a
n
t
to
t
o
existing
e
x
i
s
t
i
n
g
facilities
f
a
c
i
l
i
t
i
e
s
are
a
r
e
to
t
o
be
b
e
taken
t
a
k
e
n
into
i
n
t
o
account
a
c
c
o
u
n
t
for
f
o
r
the
t
h
e
design.
d
e
s
i
g
n
.
4.5
4
.
5
Codes
C
o
d
e
s
&
&
Standards
S
t
a
n
d
a
r
d
s
As
A
s
a
a
minimum
m
i
n
i
m
u
m
all
a
l
l
activities
a
c
t
i
v
i
t
i
e
s
shall
s
h
a
l
l
comply
c
o
m
p
l
y
with
w
i
t
h
Indonesia
I
n
d
o
n
e
s
i
a
Regulation
R
e
g
u
l
a
t
i
o
n
and
a
n
d
International
I
n
t
e
r
n
a
t
i
o
n
a
l
&
&
Company
C
o
m
p
a
n
y
Standards
S
t
a
n
d
a
r
d
s
as
a
s
detailed
d
e
t
a
i
l
e
d
in
i
n
document
d
o
c
u
m
e
n
t
ref.
r
e
f
.
[3].
[
3
]
.
4.6
4
.
6
Units
U
n
i
t
s
of
o
f
Measurements
M
e
a
s
u
r
e
m
e
n
t
s
The
T
h
e
following
f
o
l
l
o
w
i
n
g
reference
r
e
f
e
r
e
n
c
e
conditions
c
o
n
d
i
t
i
o
n
s
shall
s
h
a
l
l
be
b
e
applied
a
p
p
l
i
e
d
when
w
h
e
n
needed:
n
e
e
d
e
d
:
Reference
R
e
f
e
r
e
n
c
e
Temperature
T
e
m
p
e
r
a
t
u
r
e
[°C]
[
°
C
]
Pressure
P
r
e
s
s
u
r
e
[bara]
[
b
a
r
a
]
Standard
S
t
a
n
d
a
r
d
Conditions
C
o
n
d
i
t
i
o
n
s
15.56
1
5
.
5
6
1.013
1
.
0
1
3
Normal
N
o
r
m
a
l
Conditions
C
o
n
d
i
t
i
o
n
s
0
0
1.013
1
.
0
1
3
Table
T
a
b
l
e
1:
1
:
Reference
R
e
f
e
r
e
n
c
e
Conditions
C
o
n
d
i
t
i
o
n
s
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
The
T
h
e
units
u
n
i
t
s
of
o
f
measurement
m
e
a
s
u
r
e
m
e
n
t
will
w
i
l
l
be
b
e
generally
g
e
n
e
r
a
l
l
y
expressed
e
x
p
r
e
s
s
e
d
according
a
c
c
o
r
d
i
n
g
to
t
o
S.I.
S
.
I
.
except
e
x
c
e
p
t
for
f
o
r
the
t
h
e
following
f
o
l
l
o
w
i
n
g
differences:
d
i
f
f
e
r
e
n
c
e
s
:
Unit
U
n
i
t
Symbol
S
y
m
b
o
l
Notes
N
o
t
e
s
Temperature
T
e
m
p
e
r
a
t
u
r
e
°C
°
C
barg
b
a
r
g
Gauge
G
a
u
g
e
pressure
p
r
e
s
s
u
r
e
Pressure
P
r
e
s
s
u
r
e
bara
b
a
r
a
Absolute
A
b
s
o
l
u
t
e
pressure
p
r
e
s
s
u
r
e
Time
T
i
m
e
h
h
Reid
R
e
i
d
Vapor
V
a
p
o
r
Pressure
P
r
e
s
s
u
r
e
psi
p
s
i
(RVP)
(
R
V
P
)
True
T
r
u
e
Vapor
V
a
p
o
r
Pressure
P
r
e
s
s
u
r
e
psia
p
s
i
a
(TVP)
(
T
V
P
)
Mass
M
a
s
s
Flow
F
l
o
w
kg/h
k
g
/
h
Molar
M
o
l
a
r
Flow
F
l
o
w
kmol/h
k
m
o
l
/
h
kWe
k
W
e
Electric
E
l
e
c
t
r
i
c
Power
P
o
w
e
r
Low
L
o
w
duty
d
u
t
y
Energy
E
n
e
r
g
y
Flow
F
l
o
w
Gas
G
a
s
Flow
F
l
o
w
Liquid
L
i
q
u
i
d
Flow
F
l
o
w
MWe
M
W
e
Electric
E
l
e
c
t
r
i
c
Power
P
o
w
e
r
High
H
i
g
h
duty
d
u
t
y
10
1
0
6
6
W
W
MWth
M
W
t
h
Thermal
T
h
e
r
m
a
l
Power
P
o
w
e
r
MMSCFD
M
M
S
C
F
D
10
1
0
6
6
SCFD
S
C
F
D
MMSCMD
M
M
S
C
M
D
10
1
0
6
6
SCMD
S
C
M
D
Barrels
B
a
r
r
e
l
s
per
p
e
r
day
d
a
y
at
a
t
standard
s
t
a
n
d
a
r
d
BLPD
B
L
P
D
conditions
c
o
n
d
i
t
i
o
n
s
1
1
BLPD
B
L
P
D
=
=
0.1589873
0
.
1
5
8
9
8
7
3
m
m
3
3
/day
/
d
a
y
MMBLPD
M
M
B
L
P
D
10
1
0
6
6
BLPD
B
L
P
D
Gas
G
a
s
quantities
q
u
a
n
t
i
t
i
e
s
BSCF
B
S
C
F
10
1
0
9
9
SCF
S
C
F
Barrels
B
a
r
r
e
l
s
at
a
t
standard
s
t
a
n
d
a
r
d
conditions
c
o
n
d
i
t
i
o
n
s
Liquid
L
i
q
u
i
d
quantities
q
u
a
n
t
i
t
i
e
s
MMBBL
M
M
B
B
L
10
1
0
6
6
BBL
B
B
L
1
1
MMBBLS
M
M
B
B
L
S
=
=
158,987.3
1
5
8
,
9
8
7
.
3
m
m
3
3
ppmv
p
p
m
v
Parts
P
a
r
t
s
per
p
e
r
Million,
M
i
l
l
i
o
n
,
Volumetric
V
o
l
u
m
e
t
r
i
c
Contaminant
C
o
n
t
a
m
i
n
a
n
t
content
c
o
n
t
e
n
t
mg/Nm
m
g
/
N
m
3
3
10
1
0
-3
-
3
grams
g
r
a
m
s
per
p
e
r
normal
n
o
r
m
a
l
cubic
c
u
b
i
c
meter
m
e
t
e
r
Gas
G
a
s
Oil
O
i
l
Ratio
R
a
t
i
o
(GOR)
(
G
O
R
)
SCF/BBL
S
C
F
/
B
B
L
At
A
t
standard
s
t
a
n
d
a
r
d
conditions
c
o
n
d
i
t
i
o
n
s
Reservoir
R
e
s
e
r
v
o
i
r
permeability
p
e
r
m
e
a
b
i
l
i
t
y
mD
m
D
milli-Darcy
m
i
l
l
i
-
D
a
r
c
y
Fouling
F
o
u
l
i
n
g
Factor
F
a
c
t
o
r
m
m
2
2
–h
–
h
°C
°
C
/kcal
/
k
c
a
l
Steel
S
t
e
e
l
and
a
n
d
concrete
c
o
n
c
r
e
t
e
N/mm
N
/
m
m
strength
s
t
r
e
n
g
t
h
2
2
Diameter
D
i
a
m
e
t
e
r
of
o
f
pipe
p
i
p
e
Inches
I
n
c
h
e
s
Gas
G
a
s
Flowrate
F
l
o
w
r
a
t
e
MMSCFD
M
M
S
C
F
D
Table
T
a
b
l
e
2:
2
:
Units
U
n
i
t
s
of
o
f
Measurement
M
e
a
s
u
r
e
m
e
n
t
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
4.7
4
.
7
Coordinate
C
o
o
r
d
i
n
a
t
e
Grid
G
r
i
d
Reference
R
e
f
e
r
e
n
c
e
System
S
y
s
t
e
m
All
A
l
l
reported
r
e
p
o
r
t
e
d
coordinates
c
o
o
r
d
i
n
a
t
e
s
for
f
o
r
the
t
h
e
project
p
r
o
j
e
c
t
were
w
e
r
e
referenced
r
e
f
e
r
e
n
c
e
d
to
t
o
the
t
h
e
World
W
o
r
l
d
Geodetic
G
e
o
d
e
t
i
c
System
S
y
s
t
e
m
WGS84
W
G
S
8
4
datum
d
a
t
u
m
based
b
a
s
e
d
on
o
n
the
t
h
e
WGS84
W
G
S
8
4
spheroid,
s
p
h
e
r
o
i
d
,
and
a
n
d
are
a
r
e
projected
p
r
o
j
e
c
t
e
d
in
i
n
Universal
U
n
i
v
e
r
s
a
l
Transverse
T
r
a
n
s
v
e
r
s
e
Mercator
M
e
r
c
a
t
o
r
coordinates
c
o
o
r
d
i
n
a
t
e
s
for
f
o
r
Zone
Z
o
n
e
50
5
0
in
i
n
the
t
h
e
southern
s
o
u
t
h
e
r
n
hemisphere
h
e
m
i
s
p
h
e
r
e
(UTM
(
U
T
M
50
5
0
S).
S
)
.
Units
U
n
i
t
s
are
a
r
e
in
i
n
meters.
m
e
t
e
r
s
.
Project
P
r
o
j
e
c
t
will
w
i
l
l
use
u
s
e
the
t
h
e
same
s
a
m
e
system
s
y
s
t
e
m
of
o
f
Jangkrik
J
a
n
g
k
r
i
k
Project.
P
r
o
j
e
c
t
.
Spheroid
S
p
h
e
r
o
i
d
Spheroid
S
p
h
e
r
o
i
d
name
n
a
m
e
WGS84
W
G
S
8
4
Semi-major
S
e
m
i
-
m
a
j
o
r
axis
a
x
i
s
(a)
(
a
)
6
6
378
3
7
8
137.000
1
3
7
.
0
0
0
Semi-minor
S
e
m
i
-
m
i
n
o
r
axis
a
x
i
s
(b)
(
b
)
6
6
356
3
5
6
752.314
7
5
2
.
3
1
4
Inverse
I
n
v
e
r
s
e
flattng
f
l
a
t
t
n
g
(1/f)
(
1
/
f
)
298.257
2
9
8
.
2
5
7
223
2
2
3
563
5
6
3
Eccentricity
E
c
c
e
n
t
r
i
c
i
t
y
squared
s
q
u
a
r
e
d
(e^2)
(
e
^
2
)
0.006
0
.
0
0
6
694
6
9
4
380
3
8
0
07
0
7
Projection
P
r
o
j
e
c
t
i
o
n
Parameters
P
a
r
a
m
e
t
e
r
s
–
–
EPSG
E
P
S
G
32750
3
2
7
5
0
Projection
P
r
o
j
e
c
t
i
o
n
name
n
a
m
e
Universal
U
n
i
v
e
r
s
a
l
Transverse
T
r
a
n
s
v
e
r
s
e
Mercator
M
e
r
c
a
t
o
r
(UTM)
(
U
T
M
)
Projection
P
r
o
j
e
c
t
i
o
n
type
t
y
p
e
Transverse
T
r
a
n
s
v
e
r
s
e
Mercator
M
e
r
c
a
t
o
r
Zone
Z
o
n
e
50
5
0
South
S
o
u
t
h
Central
C
e
n
t
r
a
l
Meridian
M
e
r
i
d
i
a
n
(CM)
(
C
M
)
117°
1
1
7
°
East
E
a
s
t
Origin
O
r
i
g
i
n
latitude
l
a
t
i
t
u
d
e
0°
0
°
North
N
o
r
t
h
False
F
a
l
s
e
Easting
E
a
s
t
i
n
g
500,000
5
0
0
,
0
0
0
m
m
False
F
a
l
s
e
Northing
N
o
r
t
h
i
n
g
10,000,000
1
0
,
0
0
0
,
0
0
0
m
m
Scale
S
c
a
l
e
factor
f
a
c
t
o
r
at
a
t
CM
C
M
0.9996
0
.
9
9
9
6
Units
U
n
i
t
s
Meters
M
e
t
e
r
s
Table
T
a
b
l
e
3:
3
:
Coordinate
C
o
o
r
d
i
n
a
t
e
system
s
y
s
t
e
m
5
5
PROJECT
P
R
O
J
E
C
T
DESCRIPTION
D
E
S
C
R
I
P
T
I
O
N
5.1
5
.
1
Development
D
e
v
e
l
o
p
m
e
n
t
Scenario
S
c
e
n
a
r
i
o
The
T
h
e
Gas
G
a
s
discovery
d
i
s
c
o
v
e
r
y
well,
w
e
l
l
,
-1,
-
1
,
was
w
a
s
drilled
d
r
i
l
l
e
d
by
b
y
Gas
G
a
s
Brand
B
r
a
n
d
in
i
n
2,436’
2
,
4
3
6
’
water
w
a
t
e
r
depth
d
e
p
t
h
(
(
Indonesia
I
n
d
o
n
e
s
i
a
partner
p
a
r
t
n
e
r
at
a
t
20%)
2
0
%
)
and
a
n
d
reached
r
e
a
c
h
e
d
TD
T
D
on
o
n
June
J
u
n
e
7th
7
t
h
2002
2
0
0
2
at
a
t
-13,100’
-
1
3
,
1
0
0
’
TVDSS.
T
V
D
S
S
.
After
A
f
t
e
r
un-successful
u
n
-
s
u
c
c
e
s
s
f
u
l
proposals
p
r
o
p
o
s
a
l
s
on
o
n
the
t
h
e
Development
D
e
v
e
l
o
p
m
e
n
t
of
o
f
and
a
n
d
other
o
t
h
e
r
Gas
G
a
s
discoveries
d
i
s
c
o
v
e
r
i
e
s
in
i
n
the
t
h
e
Area,
A
r
e
a
,
Gas
G
a
s
Brand
B
r
a
n
d
released
r
e
l
e
a
s
e
d
the
t
h
e
acreage.
a
c
r
e
a
g
e
.
Indonesia
I
n
d
o
n
e
s
i
a
earned
e
a
r
n
e
d
the
t
h
e
ownership
o
w
n
e
r
s
h
i
p
of
o
f
the
t
h
e
exploration
e
x
p
l
o
r
a
t
i
o
n
and
a
n
d
exploitation
e
x
p
l
o
i
t
a
t
i
o
n
rights
r
i
g
h
t
s
on
o
n
acreage
a
c
r
e
a
g
e
again
a
g
a
i
n
after
a
f
t
e
r
successful
s
u
c
c
e
s
s
f
u
l
bidding
b
i
d
d
i
n
g
at
a
t
the
t
h
e
Indonesia’s
I
n
d
o
n
e
s
i
a
’
s
2019
2
0
1
9
bidding
b
i
d
d
i
n
g
round.
r
o
u
n
d
.
development
d
e
v
e
l
o
p
m
e
n
t
represents
r
e
p
r
e
s
e
n
t
s
an
a
n
excellent
e
x
c
e
l
l
e
n
t
synergy
s
y
n
e
r
g
y
opportunity
o
p
p
o
r
t
u
n
i
t
y
to
t
o
extend
e
x
t
e
n
d
the
t
h
e
life
l
i
f
e
of
o
f
the
t
h
e
Jangkrik
J
a
n
g
k
r
i
k
Asset:
A
s
s
e
t
:
the
t
h
e
declining
d
e
c
l
i
n
i
n
g
production
p
r
o
d
u
c
t
i
o
n
profile
p
r
o
f
i
l
e
in
i
n
Jangkrik
J
a
n
g
k
r
i
k
will
w
i
l
l
enable
e
n
a
b
l
e
to
t
o
provide
p
r
o
v
i
d
e
additional
a
d
d
i
t
i
o
n
a
l
value
v
a
l
u
e
and
a
n
d
reserves
r
e
s
e
r
v
e
s
to
t
o
.
.
The
T
h
e
project
p
r
o
j
e
c
t
is
i
s
going
g
o
i
n
g
to
t
o
provide
p
r
o
v
i
d
e
further
f
u
r
t
h
e
r
value
v
a
l
u
e
to
t
o
the
t
h
e
Government
G
o
v
e
r
n
m
e
n
t
of
o
f
Indonesia
I
n
d
o
n
e
s
i
a
and
a
n
d
to
t
o
the
t
h
e
stakeholders
s
t
a
k
e
h
o
l
d
e
r
s
along
a
l
o
n
g
the
t
h
e
gas
g
a
s
processing
p
r
o
c
e
s
s
i
n
g
and
a
n
d
commercialization
c
o
m
m
e
r
c
i
a
l
i
z
a
t
i
o
n
chain,
c
h
a
i
n
,
from
f
r
o
m
the
t
h
e
Field
F
i
e
l
d
to
t
o
the
t
h
e
Terminals,
T
e
r
m
i
n
a
l
s
,
the
t
h
e
Bontang
B
o
n
t
a
n
g
LNG
L
N
G
plant.
p
l
a
n
t
.
The
T
h
e
development
d
e
v
e
l
o
p
m
e
n
t
concept
c
o
n
c
e
p
t
of
o
f
is
i
s
subsea
s
u
b
s
e
a
tie-in
t
i
e
-
i
n
to
t
o
the
t
h
e
current
c
u
r
r
e
n
t
existing
e
x
i
s
t
i
n
g
Jangkrik
J
a
n
g
k
r
i
k
facilities
f
a
c
i
l
i
t
i
e
s
considering
c
o
n
s
i
d
e
r
i
n
g
the
t
h
e
available
a
v
a
i
l
a
b
l
e
ullage
u
l
l
a
g
e
at
a
t
the
t
h
e
late
l
a
t
e
life
l
i
f
e
of
o
f
Jangkrik
J
a
n
g
k
r
i
k
and
a
n
d
the
t
h
e
location
l
o
c
a
t
i
o
n
in
i
n
vicinity
v
i
c
i
n
i
t
y
of
o
f
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Jangkrik
J
a
n
g
k
r
i
k
Main
M
a
i
n
Clusters.
C
l
u
s
t
e
r
s
.
The
T
h
e
n.2
n
.
2
new
n
e
w
wells
w
e
l
l
s
are
a
r
e
tied-back
t
i
e
d
-
b
a
c
k
to
t
o
Jangkrik
J
a
n
g
k
r
i
k
Trunkline
T
r
u
n
k
l
i
n
e
1
1
by
b
y
means
m
e
a
n
s
of
o
f
one
o
n
e
new
n
e
w
subsea
s
u
b
s
e
a
production
p
r
o
d
u
c
t
i
o
n
flowline,
f
l
o
w
l
i
n
e
,
while
w
h
i
l
e
the
t
h
e
production
p
r
o
d
u
c
t
i
o
n
of
o
f
Jangkrik
J
a
n
g
k
r
i
k
Cluster
C
l
u
s
t
e
r
1
1
is
i
s
sent
s
e
n
t
to
t
o
Jangkrik
J
a
n
g
k
r
i
k
Cluster
C
l
u
s
t
e
r
3
3
Figure
F
i
g
u
r
e
2
2
–
–
Development
D
e
v
e
l
o
p
m
e
n
t
Scenario
S
c
e
n
a
r
i
o
6
6
GENERAL
G
E
N
E
R
A
L
LOCATION
L
O
C
A
T
I
O
N
DATA
D
A
T
A
6.1
6
.
1
CLIMATOLOGY
C
L
I
M
A
T
O
L
O
G
Y
AND
A
N
D
METOCEAN
M
E
T
O
C
E
A
N
DATA
D
A
T
A
For
F
o
r
the
t
h
e
environmental
e
n
v
i
r
o
n
m
e
n
t
a
l
data
d
a
t
a
as
a
s
seawater
s
e
a
w
a
t
e
r
temperature,
t
e
m
p
e
r
a
t
u
r
e
,
currents
c
u
r
r
e
n
t
s
and
a
n
d
waves,
w
a
v
e
s
,
ref.
r
e
f
.
to
t
o
[25].
[
2
5
]
.
6.1.1
6
.
1
.
1
Water
W
a
t
e
r
Depths
D
e
p
t
h
s
The
T
h
e
water
w
a
t
e
r
depths
d
e
p
t
h
s
in
i
n
the
t
h
e
area
a
r
e
a
ranges
r
a
n
g
e
s
from
f
r
o
m
300
3
0
0
m
m
to
t
o
1200
1
2
0
0
m
m
below
b
e
l
o
w
mean
m
e
a
n
sea
s
e
a
level.
l
e
v
e
l
.
6.1.2
6
.
1
.
2
Offshore
O
f
f
s
h
o
r
e
Plant
P
l
a
n
t
Location
L
o
c
a
t
i
o
n
Jangkrik
J
a
n
g
k
r
i
k
FPU
F
P
U
coordinates
c
o
o
r
d
i
n
a
t
e
s
Item
I
t
e
m
X
X
[m]
[
m
]
Y
Y
[m]
[
m
]
Latitude
L
a
t
i
t
u
d
e
Longitude
L
o
n
g
i
t
u
d
e
FPU
F
P
U
centre
c
e
n
t
r
e
572421
5
7
2
4
2
1
9860512
9
8
6
0
5
1
2
1°
1
°
15’
1
5
’
42,868”
4
2
,
8
6
8
”
S
S
117°
1
1
7
°
39’
3
9
’
03,499
0
3
,
4
9
9
E
E
Table
T
a
b
l
e
4:
4
:
Jangkrik
J
a
n
g
k
r
i
k
FPU
F
P
U
Coordinates
C
o
o
r
d
i
n
a
t
e
s
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
6.1.3
6
.
1
.
3
Onshore
O
n
s
h
o
r
e
Plant
P
l
a
n
t
Location
L
o
c
a
t
i
o
n
Jangkrik
J
a
n
g
k
r
i
k
Existing
E
x
i
s
t
i
n
g
ORF
O
R
F
coordinates
c
o
o
r
d
i
n
a
t
e
s
The
T
h
e
coordinates
c
o
o
r
d
i
n
a
t
e
s
of
o
f
the
t
h
e
existing
e
x
i
s
t
i
n
g
ORF
O
R
F
for
f
o
r
Jangkrik
J
a
n
g
k
r
i
k
are
a
r
e
as
a
s
here
h
e
r
e
described:
d
e
s
c
r
i
b
e
d
:
-
Latitude:
L
a
t
i
t
u
d
e
:
9899144
9
8
9
9
1
4
4
N
N
to
t
o
9899370
9
8
9
9
3
7
0
N
N
-
Longitude:
L
o
n
g
i
t
u
d
e
:
519077
5
1
9
0
7
7
E
E
to
t
o
519329
5
1
9
3
2
9
E
E
6.1.4
6
.
1
.
4
Enviromental
E
n
v
i
r
o
m
e
n
t
a
l
Data
D
a
t
a
For
F
o
r
the
t
h
e
environmental
e
n
v
i
r
o
n
m
e
n
t
a
l
data
d
a
t
a
as
a
s
seawater
s
e
a
w
a
t
e
r
temperature,
t
e
m
p
e
r
a
t
u
r
e
,
currents
c
u
r
r
e
n
t
s
and
a
n
d
waves,
w
a
v
e
s
,
refer
r
e
f
e
r
to
t
o
following
f
o
l
l
o
w
i
n
g
document
d
o
c
u
m
e
n
t
(Ref.[25]):
(
R
e
f
.
[
2
5
]
)
:
Doc
D
o
c
n°
n
°
Doc.
D
o
c
.
title
t
i
t
l
e
Revision
R
e
v
i
s
i
o
n
RP_A11111v1
R
P
_
A
1
1
1
1
1
v
1
–
–
Main
M
a
i
n
(Feb
(
F
e
b
2012)
2
0
1
2
)
SPS
S
P
S
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
Table
T
a
b
l
e
5:
5
:
Metocean
M
e
t
o
c
e
a
n
Data
D
a
t
a
Return
R
e
t
u
r
n
periods
p
e
r
i
o
d
s
for
f
o
r
which
w
h
i
c
h
oil
o
i
l
and
a
n
d
gas
g
a
s
structures
s
t
r
u
c
t
u
r
e
s
might
m
i
g
h
t
be
b
e
designed
d
e
s
i
g
n
e
d
are
a
r
e
set
s
e
t
by
b
y
national
n
a
t
i
o
n
a
l
regulation
r
e
g
u
l
a
t
i
o
n
or
o
r
guidelines.
g
u
i
d
e
l
i
n
e
s
.
For
F
o
r
the
t
h
e
typical
t
y
p
i
c
a
l
return
r
e
t
u
r
n
periods
p
e
r
i
o
d
s
refer
r
e
f
e
r
to
t
o
Company
C
o
m
p
a
n
y
Standard
S
t
a
n
d
a
r
d
28842.ENG.OFF.STD
2
8
8
4
2
.
E
N
G
.
O
F
F
.
S
T
D
“Meteo-Oceanographic
“
M
e
t
e
o
-
O
c
e
a
n
o
g
r
a
p
h
i
c
Design
D
e
s
i
g
n
Basis”.
B
a
s
i
s
”
.
6.2
6
.
2
GEOPHYSICAL
G
E
O
P
H
Y
S
I
C
A
L
AND
A
N
D
GEOTECHNICAL
G
E
O
T
E
C
H
N
I
C
A
L
DATA
D
A
T
A
6.2.1
6
.
2
.
1
Geotechnical
G
e
o
t
e
c
h
n
i
c
a
l
No
N
o
geotechnical
g
e
o
t
e
c
h
n
i
c
a
l
data
d
a
t
a
are
a
r
e
available
a
v
a
i
l
a
b
l
e
for
f
o
r
development
d
e
v
e
l
o
p
m
e
n
t
area.
a
r
e
a
.
A
A
dedicated
d
e
d
i
c
a
t
e
d
geotechnical
g
e
o
t
e
c
h
n
i
c
a
l
survey
s
u
r
v
e
y
will
w
i
l
l
be
b
e
performed
p
e
r
f
o
r
m
e
d
in
i
n
the
t
h
e
next
n
e
x
t
project
p
r
o
j
e
c
t
phases,
p
h
a
s
e
s
,
with
w
i
t
h
the
t
h
e
aim
a
i
m
to
t
o
define
d
e
f
i
n
e
the
t
h
e
soil
s
o
i
l
characterization
c
h
a
r
a
c
t
e
r
i
z
a
t
i
o
n
at
a
t
the
t
h
e
locations
l
o
c
a
t
i
o
n
s
identified
i
d
e
n
t
i
f
i
e
d
for
f
o
r
the
t
h
e
installation
i
n
s
t
a
l
l
a
t
i
o
n
of
o
f
the
t
h
e
subsea
s
u
b
s
e
a
structures,
s
t
r
u
c
t
u
r
e
s
,
flowlines
f
l
o
w
l
i
n
e
s
and
a
n
d
umbilicals.
u
m
b
i
l
i
c
a
l
s
.
6.2.2
6
.
2
.
2
Geophysical
G
e
o
p
h
y
s
i
c
a
l
No
N
o
geophysical
g
e
o
p
h
y
s
i
c
a
l
data
d
a
t
a
are
a
r
e
available
a
v
a
i
l
a
b
l
e
to
t
o
date
d
a
t
e
for
f
o
r
development
d
e
v
e
l
o
p
m
e
n
t
area.
a
r
e
a
.
A
A
dedicated
d
e
d
i
c
a
t
e
d
geophysical
g
e
o
p
h
y
s
i
c
a
l
survey
s
u
r
v
e
y
will
w
i
l
l
be
b
e
performed
p
e
r
f
o
r
m
e
d
in
i
n
the
t
h
e
next
n
e
x
t
project
p
r
o
j
e
c
t
phases,
p
h
a
s
e
s
,
with
w
i
t
h
the
t
h
e
aim
a
i
m
of
o
f
gathering
g
a
t
h
e
r
i
n
g
detailed
d
e
t
a
i
l
e
d
information
i
n
f
o
r
m
a
t
i
o
n
concerning
c
o
n
c
e
r
n
i
n
g
the
t
h
e
geomorphological
g
e
o
m
o
r
p
h
o
l
o
g
i
c
a
l
characteristics
c
h
a
r
a
c
t
e
r
i
s
t
i
c
s
of
o
f
the
t
h
e
seabed
s
e
a
b
e
d
and
a
n
d
the
t
h
e
shallow
s
h
a
l
l
o
w
subsurface.
s
u
b
s
u
r
f
a
c
e
.
The
T
h
e
survey
s
u
r
v
e
y
results
r
e
s
u
l
t
s
will
w
i
l
l
provide
p
r
o
v
i
d
e
detailed
d
e
t
a
i
l
e
d
bathymetry,
b
a
t
h
y
m
e
t
r
y
,
seabed
s
e
a
b
e
d
features
f
e
a
t
u
r
e
s
identification,
i
d
e
n
t
i
f
i
c
a
t
i
o
n
,
shallow
s
h
a
l
l
o
w
stratigraphy
s
t
r
a
t
i
g
r
a
p
h
y
and
a
n
d
related
r
e
l
a
t
e
d
potential
p
o
t
e
n
t
i
a
l
hazards.
h
a
z
a
r
d
s
.
6.2.3
6
.
2
.
3
Bathymetry
B
a
t
h
y
m
e
t
r
y
Data
D
a
t
a
No
N
o
detailed
d
e
t
a
i
l
e
d
bathymetric/morphological
b
a
t
h
y
m
e
t
r
i
c
/
m
o
r
p
h
o
l
o
g
i
c
a
l
data
d
a
t
a
are
a
r
e
available
a
v
a
i
l
a
b
l
e
for
f
o
r
the
t
h
e
project
p
r
o
j
e
c
t
area.
a
r
e
a
.
Some
S
o
m
e
preliminary
p
r
e
l
i
m
i
n
a
r
y
information
i
n
f
o
r
m
a
t
i
o
n
has
h
a
s
been
b
e
e
n
derived
d
e
r
i
v
e
d
with
w
i
t
h
a
a
reprocessing
r
e
p
r
o
c
e
s
s
i
n
g
of
o
f
a
a
3D
3
D
seismic
s
e
i
s
m
i
c
volume,
v
o
l
u
m
e
,
that
t
h
a
t
provided
p
r
o
v
i
d
e
d
a
a
low
l
o
w
resolution
r
e
s
o
l
u
t
i
o
n
(12.5m
(
1
2
.
5
m
x
x
12.5m)
1
2
.
5
m
)
bathy-morphological
b
a
t
h
y
-
m
o
r
p
h
o
l
o
g
i
c
a
l
map
m
a
p
(Figure
(
F
i
g
u
r
e
3
3
and
a
n
d
Figure
F
i
g
u
r
e
4).
4
)
.
The
T
h
e
area
a
r
e
a
is
i
s
characterized
c
h
a
r
a
c
t
e
r
i
z
e
d
by
b
y
several
s
e
v
e
r
a
l
canyons
c
a
n
y
o
n
s
(main
(
m
a
i
n
and
a
n
d
tributary),
t
r
i
b
u
t
a
r
y
)
,
visible
v
i
s
i
b
l
e
faults,
f
a
u
l
t
s
,
steep
s
t
e
e
p
slopes,
s
l
o
p
e
s
,
indented
i
n
d
e
n
t
e
d
profiles
p
r
o
f
i
l
e
s
and
a
n
d
also
a
l
s
o
isolated
i
s
o
l
a
t
e
d
mounds.
m
o
u
n
d
s
.
Water
W
a
t
e
r
depth
d
e
p
t
h
in
i
n
the
t
h
e
development
d
e
v
e
l
o
p
m
e
n
t
area
a
r
e
a
ranges
r
a
n
g
e
s
from
f
r
o
m
300
3
0
0
m
m
to
t
o
1500
1
5
0
0
m.
m
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Figure
F
i
g
u
r
e
3
3
–
–
General
G
e
n
e
r
a
l
Morphology
M
o
r
p
h
o
l
o
g
y
of
o
f
the
t
h
e
area
a
r
e
a
derived
d
e
r
i
v
e
d
from
f
r
o
m
a
a
3D
3
D
seismic
s
e
i
s
m
i
c
volume.
v
o
l
u
m
e
.
Black
B
l
a
c
k
Circle
C
i
r
c
l
e
defines
d
e
f
i
n
e
s
the
t
h
e
development
d
e
v
e
l
o
p
m
e
n
t
area.
a
r
e
a
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Figure
F
i
g
u
r
e
4
4
–
–
General
G
e
n
e
r
a
l
Morphology
M
o
r
p
h
o
l
o
g
y
of
o
f
the
t
h
e
area
a
r
e
a
derived
d
e
r
i
v
e
d
from
f
r
o
m
a
a
3D
3
D
seismic
s
e
i
s
m
i
c
volume.
v
o
l
u
m
e
.
Detail
D
e
t
a
i
l
of
o
f
the
t
h
e
area
a
r
e
a
of
o
f
interest
i
n
t
e
r
e
s
t
6.2.4
6
.
2
.
4
Geohazard
G
e
o
h
a
z
a
r
d
Assessment
A
s
s
e
s
s
m
e
n
t
No
N
o
geohazard
g
e
o
h
a
z
a
r
d
studies
s
t
u
d
i
e
s
have
h
a
v
e
been
b
e
e
n
performed
p
e
r
f
o
r
m
e
d
with
w
i
t
h
focus
f
o
c
u
s
on
o
n
development
d
e
v
e
l
o
p
m
e
n
t
area.
a
r
e
a
.
6.2.5
6
.
2
.
5
Earthquake
E
a
r
t
h
q
u
a
k
e
Data
D
a
t
a
ISO
I
S
O
19901-2
1
9
9
0
1
-
2
shall
s
h
a
l
l
be
b
e
considered
c
o
n
s
i
d
e
r
e
d
for
f
o
r
the
t
h
e
design
d
e
s
i
g
n
of
o
f
subsea
s
u
b
s
e
a
structures
s
t
r
u
c
t
u
r
e
s
and
a
n
d
foundations
f
o
u
n
d
a
t
i
o
n
s
7
7
RESERVOIR
R
E
S
E
R
V
O
I
R
MANAGEMENT
M
A
N
A
G
E
M
E
N
T
BASIS
B
A
S
I
S
7.1
7
.
1
Main
M
a
i
n
Reservoir
R
e
s
e
r
v
o
i
r
Data
D
a
t
a
The
T
h
e
primary
p
r
i
m
a
r
y
reservoir
r
e
s
e
r
v
o
i
r
discovered
d
i
s
c
o
v
e
r
e
d
in
i
n
Field
F
i
e
l
d
is
i
s
T-090
T
-
0
9
0
(equivalent
(
e
q
u
i
v
a
l
e
n
t
to
t
o
3130
3
1
3
0
based
b
a
s
e
d
on
o
n
previous
p
r
e
v
i
o
u
s
Gas
G
a
s
Brand
B
r
a
n
d
nomenclature)
n
o
m
e
n
c
l
a
t
u
r
e
)
and
a
n
d
it
i
t
was
w
a
s
penetrated
p
e
n
e
t
r
a
t
e
d
at
a
t
a
a
depth
d
e
p
t
h
of
o
f
approximately
a
p
p
r
o
x
i
m
a
t
e
l
y
-2,400
-
2
,
4
0
0
to
t
o
-2,600
-
2
,
6
0
0
meter
m
e
t
e
r
subsea
s
u
b
s
e
a
true
t
r
u
e
vertical
v
e
r
t
i
c
a
l
depth
d
e
p
t
h
(TVDSS).
(
T
V
D
S
S
)
.
Secondary
S
e
c
o
n
d
a
r
y
reservoirs
r
e
s
e
r
v
o
i
r
s
are
a
r
e
T-088-T-086
T
-
0
8
8
-
T
-
0
8
6
(equivalent
(
e
q
u
i
v
a
l
e
n
t
to
t
o
3140
3
1
4
0
and
a
n
d
3150
3
1
5
0
based
b
a
s
e
d
on
o
n
previous
p
r
e
v
i
o
u
s
Gas
G
a
s
Brand
B
r
a
n
d
nomenclature
n
o
m
e
n
c
l
a
t
u
r
e
)
)
and
a
n
d
T-084
T
-
0
8
4
Segment-1
S
e
g
m
e
n
t
-
1
(equivalent
(
e
q
u
i
v
a
l
e
n
t
to
t
o
3170
3
1
7
0
based
b
a
s
e
d
on
o
n
previous
p
r
e
v
i
o
u
s
Gas
G
a
s
Brand
B
r
a
n
d
nomenclature).
n
o
m
e
n
c
l
a
t
u
r
e
)
.
field
f
i
e
l
d
is
i
s
a
a
Pliocene
P
l
i
o
c
e
n
e
turbidite
t
u
r
b
i
d
i
t
e
deposited
d
e
p
o
s
i
t
e
d
3.5
3
.
5
million
m
i
l
l
i
o
n
years
y
e
a
r
s
ago
a
g
o
as
a
s
toe-of-slope
t
o
e
-
o
f
-
s
l
o
p
e
fans
f
a
n
s
that
t
h
a
t
draped
d
r
a
p
e
d
over
o
v
e
r
an
a
n
anticlinal
a
n
t
i
c
l
i
n
a
l
structure
s
t
r
u
c
t
u
r
e
that
t
h
a
t
is
i
s
part
p
a
r
t
of
o
f
the
t
h
e
greater
g
r
e
a
t
e
r
Gendalo
G
e
n
d
a
l
o
Hub
H
u
b
anticline.
a
n
t
i
c
l
i
n
e
.
The
T
h
e
trap
t
r
a
p
at
a
t
the
t
h
e
field
f
i
e
l
d
is
i
s
stratigraphic,
s
t
r
a
t
i
g
r
a
p
h
i
c
,
formed
f
o
r
m
e
d
by
b
y
the
t
h
e
pinch-out
p
i
n
c
h
-
o
u
t
of
o
f
Pliocene
P
l
i
o
c
e
n
e
turbidites
t
u
r
b
i
d
i
t
e
s
up-dip
u
p
-
d
i
p
into
i
n
t
o
a
a
slope
s
l
o
p
e
valley.
v
a
l
l
e
y
.
The
T
h
e
T-090
T
-
0
9
0
reservoir
r
e
s
e
r
v
o
i
r
is
i
s
the
t
h
e
primary
p
r
i
m
a
r
y
gas
g
a
s
accumulation
a
c
c
u
m
u
l
a
t
i
o
n
and
a
n
d
contains
c
o
n
t
a
i
n
s
approximately
a
p
p
r
o
x
i
m
a
t
e
l
y
74%
7
4
%
of
o
f
the
t
h
e
total
t
o
t
a
l
gas-in-place.
g
a
s
-
i
n
-
p
l
a
c
e
.
The
T
h
e
amplitude,
a
m
p
l
i
t
u
d
e
,
ESP,
E
S
P
,
and
a
n
d
SpecD
S
p
e
c
D
maps
m
a
p
s
clearly
c
l
e
a
r
l
y
show
s
h
o
w
the
t
h
e
toe-of-slope
t
o
e
-
o
f
-
s
l
o
p
e
fan
f
a
n
geometry
g
e
o
m
e
t
r
y
and
a
n
d
the
t
h
e
opng
o
p
n
g
neck
n
e
c
k
of
o
f
the
t
h
e
slope
s
l
o
p
e
valley
v
a
l
l
e
y
feeding
f
e
e
d
i
n
g
the
t
h
e
fan
f
a
n
from
f
r
o
m
the
t
h
e
northwest.
n
o
r
t
h
w
e
s
t
.
Based
B
a
s
e
d
on
o
n
the
t
h
e
revised
r
e
v
i
s
e
d
depositional
d
e
p
o
s
i
t
i
o
n
a
l
model
m
o
d
e
l
is
i
s
characterized
c
h
a
r
a
c
t
e
r
i
z
e
d
by
b
y
a
a
channel-attached
c
h
a
n
n
e
l
-
a
t
t
a
c
h
e
d
fan
f
a
n
system
s
y
s
t
e
m
with
w
i
t
h
presence
p
r
e
s
e
n
c
e
of
o
f
potential
p
o
t
e
n
t
i
a
l
barriers.
b
a
r
r
i
e
r
s
.
The
T
h
e
T-090
T
-
0
9
0
package
p
a
c
k
a
g
e
thins
t
h
i
n
s
up-dip
u
p
-
d
i
p
into
i
n
t
o
the
t
h
e
slope
s
l
o
p
e
valley
v
a
l
l
e
y
and,
a
n
d
,
while
w
h
i
l
e
the
t
h
e
entire
e
n
t
i
r
e
package
p
a
c
k
a
g
e
correlates
c
o
r
r
e
l
a
t
e
s
well
w
e
l
l
seismically,
s
e
i
s
m
i
c
a
l
l
y
,
the
t
h
e
internal
i
n
t
e
r
n
a
l
stratigraphic
s
t
r
a
t
i
g
r
a
p
h
i
c
complexities
c
o
m
p
l
e
x
i
t
i
e
s
are
a
r
e
not
n
o
t
well
w
e
l
l
defined.
d
e
f
i
n
e
d
.
The
T
h
e
depositional
d
e
p
o
s
i
t
i
o
n
a
l
lobes
l
o
b
e
s
show
s
h
o
w
a
a
compensational
c
o
m
p
e
n
s
a
t
i
o
n
a
l
stacking;
s
t
a
c
k
i
n
g
;
these
t
h
e
s
e
events
e
v
e
n
t
s
often
o
f
t
e
n
can
c
a
n
amalgamate
a
m
a
l
g
a
m
a
t
e
laterally
l
a
t
e
r
a
l
l
y
making
m
a
k
i
n
g
difficult
d
i
f
f
i
c
u
l
t
to
t
o
define
d
e
f
i
n
e
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
architecture.
a
r
c
h
i
t
e
c
t
u
r
e
.
No
N
o
GWC
G
W
C
was
w
a
s
recognized
r
e
c
o
g
n
i
z
e
d
at
a
t
well
w
e
l
l
locations;
l
o
c
a
t
i
o
n
s
;
RMS
R
M
S
amplitude
a
m
p
l
i
t
u
d
e
shut
s
h
u
t
off
o
f
f
suggests
s
u
g
g
e
s
t
s
a
a
contact
c
o
n
t
a
c
t
near
n
e
a
r
to
t
o
-2560
-
2
5
6
0
mssl.
m
s
s
l
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
The
T
h
e
T-088/T-086
T
-
0
8
8
/
T
-
0
8
6
reservoirs
r
e
s
e
r
v
o
i
r
s
was
w
a
s
encountered
e
n
c
o
u
n
t
e
r
e
d
30-40
3
0
-
4
0
meters
m
e
t
e
r
s
below
b
e
l
o
w
the
t
h
e
primary
p
r
i
m
a
r
y
reservoir.
r
e
s
e
r
v
o
i
r
.
The
T
h
e
reservoir
r
e
s
e
r
v
o
i
r
consists
c
o
n
s
i
s
t
s
of
o
f
two
t
w
o
distinct
d
i
s
t
i
n
c
t
sand
s
a
n
d
bodies
b
o
d
i
e
s
in
i
n
the
t
h
e
-1
-
1
and
a
n
d
Gendalo-4
G
e
n
d
a
l
o
-
4
wells
w
e
l
l
s
that
t
h
a
t
share
s
h
a
r
e
the
t
h
e
same
s
a
m
e
gas
g
a
s
and
a
n
d
water
w
a
t
e
r
gradient
g
r
a
d
i
e
n
t
based
b
a
s
e
d
on
o
n
MDT
M
D
T
pressure
p
r
e
s
s
u
r
e
data.
d
a
t
a
.
The
T
h
e
up-dip
u
p
-
d
i
p
-1
-
1
well
w
e
l
l
found
f
o
u
n
d
a
a
GWC
G
W
C
@
@
-2,556
-
2
,
5
5
6
meter
m
e
t
e
r
while
w
h
i
l
e
the
t
h
e
down-dip
d
o
w
n
-
d
i
p
Gendalo-4
G
e
n
d
a
l
o
-
4
was
w
a
s
found
f
o
u
n
d
wet.
w
e
t
.
GWC
G
W
C
at
a
t
-1
-
1
well
w
e
l
l
position
p
o
s
i
t
i
o
n
was
w
a
s
confirmed
c
o
n
f
i
r
m
e
d
by
b
y
the
t
h
e
-1
-
1
and
a
n
d
Gendalo-4
G
e
n
d
a
l
o
-
4
pressure
p
r
e
s
s
u
r
e
gradient
g
r
a
d
i
e
n
t
analysis.
a
n
a
l
y
s
i
s
.
T088-
T
0
8
8
-
T086
T
0
8
6
seems
s
e
e
m
s
to
t
o
be
b
e
a
a
more
m
o
r
e
channelized
c
h
a
n
n
e
l
i
z
e
d
systems
s
y
s
t
e
m
s
with
w
i
t
h
two
t
w
o
main
m
a
i
n
fairways
f
a
i
r
w
a
y
s
oriented
o
r
i
e
n
t
e
d
NW-S
N
W
-
S
and
a
n
d
NW-SE.
N
W
-
S
E
.
In
I
n
the
t
h
e
SE
S
E
area
a
r
e
a
probably,
p
r
o
b
a
b
l
y
,
there
t
h
e
r
e
are
a
r
e
some
s
o
m
e
features
f
e
a
t
u
r
e
s
that
t
h
a
t
could
c
o
u
l
d
be
b
e
related
r
e
l
a
t
e
d
to
t
o
bottom
b
o
t
t
o
m
currents
c
u
r
r
e
n
t
s
reworking
r
e
w
o
r
k
i
n
g
or
o
r
crevasse
c
r
e
v
a
s
s
e
splays.
s
p
l
a
y
s
.
The
T
h
e
T-084
T
-
0
8
4
is
i
s
the
t
h
e
basal
b
a
s
a
l
sand
s
a
n
d
in
i
n
the
t
h
e
Pliocene
P
l
i
o
c
e
n
e
slope
s
l
o
p
e
valley
v
a
l
l
e
y
depositional
d
e
p
o
s
i
t
i
o
n
a
l
system.
s
y
s
t
e
m
.
RMS
R
M
S
amplitude
a
m
p
l
i
t
u
d
e
extraction
e
x
t
r
a
c
t
i
o
n
suggests
s
u
g
g
e
s
t
s
a
a
possible
p
o
s
s
i
b
l
e
channels
c
h
a
n
n
e
l
s
systems
s
y
s
t
e
m
s
in
i
n
-1
-
1
area
a
r
e
a
and
a
n
d
a
a
stratigraphic
s
t
r
a
t
i
g
r
a
p
h
i
c
expansion
e
x
p
a
n
s
i
o
n
with
w
i
t
h
depositional
d
e
p
o
s
i
t
i
o
n
a
l
lobes
l
o
b
e
s
in
i
n
the
t
h
e
area
a
r
e
a
south
s
o
u
t
h
of
o
f
Gendalo-4.
G
e
n
d
a
l
o
-
4
.
T-084
T
-
0
8
4
was
w
a
s
found
f
o
u
n
d
gas
g
a
s
bearing
b
e
a
r
i
n
g
in
i
n
-1
-
1
well,
w
e
l
l
,
while
w
h
i
l
e
Gendalo-4
G
e
n
d
a
l
o
-
4
didn’t
d
i
d
n
’
t
reach
r
e
a
c
h
this
t
h
i
s
target.
t
a
r
g
e
t
.
-1
-
1
well
w
e
l
l
encountered
e
n
c
o
u
n
t
e
r
e
d
a
a
GWC
G
W
C
at
a
t
-2,626
-
2
,
6
2
6
m
m
TVDSS
T
V
D
S
S
which
w
h
i
c
h
is
i
s
confirmed
c
o
n
f
i
r
m
e
d
by
b
y
MDT
M
D
T
pressure
p
r
e
s
s
u
r
e
points.
p
o
i
n
t
s
.
-1
-
1
MDT
M
D
T
pressure
p
r
e
s
s
u
r
e
analysis
a
n
a
l
y
s
i
s
shows
s
h
o
w
s
that
t
h
a
t
the
t
h
e
T-084
T
-
0
8
4
is
i
s
over-pressured
o
v
e
r
-
p
r
e
s
s
u
r
e
d
relative
r
e
l
a
t
i
v
e
to
t
o
the
t
h
e
shallower
s
h
a
l
l
o
w
e
r
reservoirs.
r
e
s
e
r
v
o
i
r
s
.
Based
B
a
s
e
d
on
o
n
the
t
h
e
petrophysichal
p
e
t
r
o
p
h
y
s
i
c
h
a
l
evaluation
e
v
a
l
u
a
t
i
o
n
of
o
f
the
t
h
e
explorative
e
x
p
l
o
r
a
t
i
v
e
wells
w
e
l
l
s
done
d
o
n
e
in
i
n
2020,
2
0
2
0
,
as
a
s
part
p
a
r
t
of
o
f
the
t
h
e
Integrated
I
n
t
e
g
r
a
t
e
d
Reservoir
R
e
s
e
r
v
o
i
r
Study,
S
t
u
d
y
,
-1
-
1
and
a
n
d
Gendalo-4
G
e
n
d
a
l
o
-
4
penetrated
p
e
n
e
t
r
a
t
e
d
the
t
h
e
T90,
T
9
0
,
T088-T086
T
0
8
8
-
T
0
8
6
and
a
n
d
T084
T
0
8
4
encountering
e
n
c
o
u
n
t
e
r
i
n
g
the
t
h
e
thickness
t
h
i
c
k
n
e
s
s
and
a
n
d
founding
f
o
u
n
d
i
n
g
petrophysichal
p
e
t
r
o
p
h
y
s
i
c
h
a
l
properties
p
r
o
p
e
r
t
i
e
s
as
a
s
indicated
i
n
d
i
c
a
t
e
d
in
i
n
table
t
a
b
l
e
below.
b
e
l
o
w
.
Wells
W
e
l
l
s
Reservoir
R
e
s
e
r
v
o
i
r
Gross
G
r
o
s
s
Interva
I
n
t
e
r
v
a
l
l
m
m
TVD
T
V
D
Net
N
e
t
Reservoi
R
e
s
e
r
v
o
i
r
r
m
m
TVD
T
V
D
NTG
N
T
G
Reservoi
R
e
s
e
r
v
o
i
r
r
Avg.
A
v
g
.
PHIE
P
H
I
E
Reservoi
R
e
s
e
r
v
o
i
r
r
Avg.
A
v
g
.
Swe
S
w
e
Pay
P
a
y
Avg.
A
v
g
.
Perm.
P
e
r
m
.
Reservoir
R
e
s
e
r
v
o
i
r
-1
-
1
23
2
3
21
2
1
0.9
0
.
9
0.25
0
.
2
5
0.42
0
.
4
2
76
7
6
mD
m
D
T90
T
9
0
Gendalo-4
G
e
n
d
a
l
o
-
4
54
5
4
43
4
3
0.8
0
.
8
0.26
0
.
2
6
0.45
0
.
4
5
129
1
2
9
mD
m
D
-1
-
1
72
7
2
34
3
4
0.46
0
.
4
6
0.24
0
.
2
4
0.48
0
.
4
8
109
1
0
9
mD
m
D
T88/86
T
8
8
/
8
6
Gendalo-4
G
e
n
d
a
l
o
-
4
55
5
5
24
2
4
0.43
0
.
4
3
0.25
0
.
2
5
-
-
177
1
7
7
mD
m
D
-1
-
1
21
2
1
20
2
0
0.94
0
.
9
4
0.30
0
.
3
0
0.16
0
.
1
6
288
2
8
8
mD
m
D
T84
T
8
4
Gendalo-4
G
e
n
d
a
l
o
-
4
Not
N
o
t
Penetrated
P
e
n
e
t
r
a
t
e
d
Table
T
a
b
l
e
6
6
–
–
Summary
S
u
m
m
a
r
y
of
o
f
the
t
h
e
average
a
v
e
r
a
g
e
properties
p
r
o
p
e
r
t
i
e
s
of
o
f
reservoirs,
r
e
s
e
r
v
o
i
r
s
,
based
b
a
s
e
d
on
o
n
the
t
h
e
explorative
e
x
p
l
o
r
a
t
i
v
e
wells.
w
e
l
l
s
.
A
A
3D
3
D
model
m
o
d
e
l
was
w
a
s
built
b
u
i
l
t
to
t
o
capture
c
a
p
t
u
r
e
all
a
l
l
the
t
h
e
correctly
c
o
r
r
e
c
t
l
y
scaled
s
c
a
l
e
d
reservoir
r
e
s
e
r
v
o
i
r
characteristics
c
h
a
r
a
c
t
e
r
i
s
t
i
c
s
that
t
h
a
t
have
h
a
v
e
been
b
e
e
n
identified
i
d
e
n
t
i
f
i
e
d
from
f
r
o
m
seismic,
s
e
i
s
m
i
c
,
well,
w
e
l
l
,
and
a
n
d
analog
a
n
a
l
o
g
data,
d
a
t
a
,
and
a
n
d
delivers
d
e
l
i
v
e
r
s
an
a
n
original
o
r
i
g
i
n
a
l
gas-in-place.
g
a
s
-
i
n
-
p
l
a
c
e
.
The
T
h
e
volumetric
v
o
l
u
m
e
t
r
i
c
field
f
i
e
l
d
average
a
v
e
r
a
g
e
properties
p
r
o
p
e
r
t
i
e
s
are
a
r
e
reported
r
e
p
o
r
t
e
d
in
i
n
the
t
h
e
table
t
a
b
l
e
below.
b
e
l
o
w
.
Avg
A
v
g
NTG
N
T
G
Avg
A
v
g
Porosity
P
o
r
o
s
i
t
y
Avg
A
v
g
SW
S
W
Case
C
a
s
e
[%]
[
%
]
[%]
[
%
]
[%]
[
%
]
Reference
R
e
f
e
r
e
n
c
e
Case
C
a
s
e
67%
6
7
%
27%
2
7
%
39%
3
9
%
T090
T
0
9
0
75%
7
5
%
27%
2
7
%
41%
4
1
%
T088-086
T
0
8
8
-
0
8
6
43%
4
3
%
25%
2
5
%
44%
4
4
%
T084
T
0
8
4
83%
8
3
%
33%
3
3
%
20%
2
0
%
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Table
T
a
b
l
e
7
7
–
–
Average
A
v
e
r
a
g
e
reservoir
r
e
s
e
r
v
o
i
r
properties
p
r
o
p
e
r
t
i
e
s
from
f
r
o
m
volumetrics
v
o
l
u
m
e
t
r
i
c
s
PVT
P
V
T
experiments
e
x
p
e
r
i
m
e
n
t
s
are
a
r
e
not
n
o
t
available
a
v
a
i
l
a
b
l
e
in
i
n
field.
f
i
e
l
d
.
In
I
n
order
o
r
d
e
r
to
t
o
characterize
c
h
a
r
a
c
t
e
r
i
z
e
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid,
f
l
u
i
d
,
gas
g
a
s
composition
c
o
m
p
o
s
i
t
i
o
n
and
a
n
d
CGR
C
G
R
from
f
r
o
m
MDT
M
D
T
sampling
s
a
m
p
l
i
n
g
have
h
a
v
e
been
b
e
e
n
considered.
c
o
n
s
i
d
e
r
e
d
.
The
T
h
e
reference
r
e
f
e
r
e
n
c
e
sample,
s
a
m
p
l
e
,
taken
t
a
k
e
n
in
i
n
T090
T
0
9
0
level
l
e
v
e
l
at
a
t
a
a
depth
d
e
p
t
h
of
o
f
8158
8
1
5
8
ft
f
t
(2486.6
(
2
4
8
6
.
6
m),
m
)
,
pressure
p
r
e
s
s
u
r
e
of
o
f
3903
3
9
0
3
Psia
P
s
i
a
and
a
n
d
a
a
temperature
t
e
m
p
e
r
a
t
u
r
e
of
o
f
151
1
5
1
°F,
°
F
,
has
h
a
s
a
a
C1
C
1
content
c
o
n
t
e
n
t
of
o
f
98.3%,
9
8
.
3
%
,
a
a
gas
g
a
s
gravity
g
r
a
v
i
t
y
of
o
f
0.58
0
.
5
8
and
a
n
d
a
a
CGR
C
G
R
of
o
f
5.8
5
.
8
Stb/MMscf.
S
t
b
/
M
M
s
c
f
.
The
T
h
e
data
d
a
t
a
have
h
a
v
e
matched
m
a
t
c
h
e
d
by
b
y
means
m
e
a
n
s
of
o
f
an
a
n
equation
e
q
u
a
t
i
o
n
of
o
f
state
s
t
a
t
e
in
i
n
PVTi
P
V
T
i
software.
s
o
f
t
w
a
r
e
.
The
T
h
e
T90
T
9
0
PVT
P
V
T
has
h
a
s
been
b
e
e
n
considered
c
o
n
s
i
d
e
r
e
d
for
f
o
r
the
t
h
e
other
o
t
h
e
r
levels
l
e
v
e
l
s
of
o
f
the
t
h
e
field.
f
i
e
l
d
.
Properties
P
r
o
p
e
r
t
i
e
s
Value
V
a
l
u
e
Reservoir
R
e
s
e
r
v
o
i
r
Pressure
P
r
e
s
s
u
r
e
(bara)
(
b
a
r
a
)
270-272
2
7
0
-
2
7
2
Reservoir
R
e
s
e
r
v
o
i
r
Temperature
T
e
m
p
e
r
a
t
u
r
e
(°C)
(
°
C
)
73-74
7
3
-
7
4
Table
T
a
b
l
e
8
8
–
–
Reservoir
R
e
s
e
r
v
o
i
r
Fluid
F
l
u
i
d
Conditions
C
o
n
d
i
t
i
o
n
s
and
a
n
d
Properties
P
r
o
p
e
r
t
i
e
s
-2
-
2
well
w
e
l
l
was
w
a
s
recently
r
e
c
e
n
t
l
y
drilled
d
r
i
l
l
e
d
(May
(
M
a
y
2021)
2
0
2
1
)
and
a
n
d
preliminary
p
r
e
l
i
m
i
n
a
r
y
petrophysichal
p
e
t
r
o
p
h
y
s
i
c
h
a
l
analysis
a
n
a
l
y
s
i
s
confirms
c
o
n
f
i
r
m
s
the
t
h
e
good
g
o
o
d
reservoir
r
e
s
e
r
v
o
i
r
quality
q
u
a
l
i
t
y
of
o
f
the
t
h
e
primary
p
r
i
m
a
r
y
target
t
a
r
g
e
t
(T-090),
(
T
-
0
9
0
)
,
on
o
n
which
w
h
i
c
h
the
t
h
e
development
d
e
v
e
l
o
p
m
e
n
t
of
o
f
the
t
h
e
field
f
i
e
l
d
is
i
s
based.
b
a
s
e
d
.
PVT
P
V
T
and
a
n
d
core
c
o
r
e
analysis
a
n
a
l
y
s
i
s
results
r
e
s
u
l
t
s
are
a
r
e
not
n
o
t
yet
y
e
t
available
a
v
a
i
l
a
b
l
e
at
a
t
the
t
h
e
time
t
i
m
e
of
o
f
the
t
h
e
present
p
r
e
s
e
n
t
BoD.
B
o
D
.
7.2
7
.
2
Reservoir
R
e
s
e
r
v
o
i
r
Fluid
F
l
u
i
d
Composition
C
o
m
p
o
s
i
t
i
o
n
The
T
h
e
reservoir
r
e
s
e
r
v
o
i
r
pressure,
p
r
e
s
s
u
r
e
,
temperature
t
e
m
p
e
r
a
t
u
r
e
and
a
n
d
fluid
f
l
u
i
d
properties
p
r
o
p
e
r
t
i
e
s
for
f
o
r
reservoir
r
e
s
e
r
v
o
i
r
are
a
r
e
reported
r
e
p
o
r
t
e
d
at
a
t
para.7.1,
p
a
r
a
.
7
.
1
,
while
w
h
i
l
e
its
i
t
s
compositions
c
o
m
p
o
s
i
t
i
o
n
s
is
i
s
tabulated
t
a
b
u
l
a
t
e
d
as
a
s
follows
f
o
l
l
o
w
s
.
.
Component
C
o
m
p
o
n
e
n
t
%mol
%
m
o
l
MW
M
W
Specific
S
p
e
c
i
f
i
c
Gravity
G
r
a
v
i
t
y
Critical
C
r
i
t
i
c
a
l
Temp.
T
e
m
p
.
°C
°
C
Critical
C
r
i
t
i
c
a
l
Pressure
P
r
e
s
s
u
r
e
bara
b
a
r
a
Acentric
A
c
e
n
t
r
i
c
factor
f
a
c
t
o
r
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
boiling
b
o
i
l
i
n
g
Temp.
T
e
m
p
.
°C
°
C
Critical
C
r
i
t
i
c
a
l
vol.
v
o
l
.
cm3/mol
c
m
3
/
m
o
l
N2
N
2
0.040
0
.
0
4
0
28.01
2
8
.
0
1
-147.0
-
1
4
7
.
0
33.9
3
3
.
9
0.0400
0
.
0
4
0
0
-195.8
-
1
9
5
.
8
89.8
8
9
.
8
CO2
C
O
2
0.919
0
.
9
1
9
44.01
4
4
.
0
1
31.1
3
1
.
1
73.8
7
3
.
8
0.2250
0
.
2
2
5
0
-78.5
-
7
8
.
5
94.0
9
4
.
0
C1
C
1
98.200
9
8
.
2
0
0
16.04
1
6
.
0
4
-82.6
-
8
2
.
6
46.0
4
6
.
0
0.0080
0
.
0
0
8
0
-161.6
-
1
6
1
.
6
99.0
9
9
.
0
C2
C
2
0.200
0
.
2
0
0
30.07
3
0
.
0
7
32.3
3
2
.
3
48.8
4
8
.
8
0.0980
0
.
0
9
8
0
-88.6
-
8
8
.
6
148.0
1
4
8
.
0
C3
C
3
0.090
0
.
0
9
0
44.10
4
4
.
1
0
96.7
9
6
.
7
42.5
4
2
.
5
0.1520
0
.
1
5
2
0
-42.5
-
4
2
.
5
203.0
2
0
3
.
0
i
i
C4
C
4
0.020
0
.
0
2
0
58.12
5
8
.
1
2
135.0
1
3
5
.
0
36.5
3
6
.
5
0.1760
0
.
1
7
6
0
-11.8
-
1
1
.
8
263.0
2
6
3
.
0
nC4
n
C
4
0.020
0
.
0
2
0
58.12
5
8
.
1
2
152.1
1
5
2
.
1
38.0
3
8
.
0
0.1930
0
.
1
9
3
0
0.5
0
.
5
255.0
2
5
5
.
0
i
i
C5
C
5
0.010
0
.
0
1
0
72.15
7
2
.
1
5
187.3
1
8
7
.
3
33.8
3
3
.
8
0.2270
0
.
2
2
7
0
27.9
2
7
.
9
306.0
3
0
6
.
0
nC5
n
C
5
0.010
0
.
0
1
0
72.15
7
2
.
1
5
196.5
1
9
6
.
5
33.7
3
3
.
7
0.2510
0
.
2
5
1
0
36.1
3
6
.
1
304.0
3
0
4
.
0
C6
C
6
0.011
0
.
0
1
1
86.18
8
6
.
1
8
0.664
0
.
6
6
4
234.3
2
3
4
.
3
29.7
2
9
.
7
0.2960
0
.
2
9
6
0
68.8
6
8
.
8
370.0
3
7
0
.
0
C7
C
7
0.097
0
.
0
9
7
96.00
9
6
.
0
0
0.702
0
.
7
0
2
260.7
2
6
0
.
7
28.7
2
8
.
7
0.3371
0
.
3
3
7
1
92.0
9
2
.
0
521.9
5
2
1
.
9
C8
C
8
0.079
0
.
0
7
9
107.00
1
0
7
.
0
0
0.730
0
.
7
3
0
282.3
2
8
2
.
3
26.8
2
6
.
8
0.3740
0
.
3
7
4
0
116.8
1
1
6
.
8
532.0
5
3
2
.
0
C9
C
9
0.065
0
.
0
6
5
121.00
1
2
1
.
0
0
0.754
0
.
7
5
4
306.9
3
0
6
.
9
24.6
2
4
.
6
0.4202
0
.
4
2
0
2
142.3
1
4
2
.
3
561.5
5
6
1
.
5
C10
C
1
0
0.052
0
.
0
5
2
134.00
1
3
4
.
0
0
0.776
0
.
7
7
6
328.2
3
2
8
.
2
23.5
2
3
.
5
0.4627
0
.
4
6
2
7
165.9
1
6
5
.
9
592.4
5
9
2
.
4
C11
C
1
1
0.041
0
.
0
4
1
147.00
1
4
7
.
0
0
0.795
0
.
7
9
5
348.0
3
4
8
.
0
21.8
2
1
.
8
0.5007
0
.
5
0
0
7
187.3
1
8
7
.
3
628.0
6
2
8
.
0
C12
C
1
2
0.031
0
.
0
3
1
161.00
1
6
1
.
0
0
0.813
0
.
8
1
3
368.1
3
6
8
.
1
20.6
2
0
.
6
0.5428
0
.
5
4
2
8
208.4
2
0
8
.
4
672.2
6
7
2
.
2
C13
C
1
3
0.023
0
.
0
2
3
175.00
1
7
5
.
0
0
0.829
0
.
8
2
9
387.1
3
8
7
.
1
19.7
1
9
.
7
0.5837
0
.
5
8
3
7
227.3
2
2
7
.
3
719.9
7
1
9
.
9
Table
T
a
b
l
e
9
9
–
–
Reservoir
R
e
s
e
r
v
o
i
r
Fluid
F
l
u
i
d
Composition
C
o
m
p
o
s
i
t
i
o
n
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
7.3
7
.
3
Production
P
r
o
d
u
c
t
i
o
n
Capacity
C
a
p
a
c
i
t
y
Overview
O
v
e
r
v
i
e
w
and
a
n
d
Profiles
P
r
o
f
i
l
e
s
Two
T
w
o
reference
r
e
f
e
r
e
n
c
e
Production
P
r
o
d
u
c
t
i
o
n
profiles
p
r
o
f
i
l
e
s
are
a
r
e
reported
r
e
p
o
r
t
e
d
below:
b
e
l
o
w
:
-
-
Constrained
C
o
n
s
t
r
a
i
n
e
d
case
c
a
s
e
(max
(
m
a
x
trunkline
t
r
u
n
k
l
i
n
e
flowrate
f
l
o
w
r
a
t
e
230
2
3
0
MMSCFD)
M
M
S
C
F
D
)
Well
W
e
l
l
Gas
G
a
s
Rate
R
a
t
e
(MMSCFD)
(
M
M
S
C
F
D
)
Well
W
e
l
l
Cond
C
o
n
d
Rate
R
a
t
e
(STBD)
(
S
T
B
D
)
Well
W
e
l
l
Water
W
a
t
e
r
Rate
R
a
t
e
(STBD)
(
S
T
B
D
)
Year
Y
e
a
r
Month
M
o
n
t
h
-3
-
3
-4
-
4
-3
-
3
-4
-
4
-3
-
3
-4
-
4
2026
2
0
2
6
2027
2
0
2
7
2028
2
0
2
8
Jan
J
a
n
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Feb
F
e
b
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Mar
M
a
r
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Apr
A
p
r
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
May
M
a
y
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Jun
J
u
n
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Jul
J
u
l
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Aug
A
u
g
4
4
4
4
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Sep
S
e
p
100
1
0
0
100
1
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Oct
O
c
t
107
1
0
7
107
1
0
7
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Nov
N
o
v
110
1
1
0
111
1
1
1
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Dec
D
e
c
115
1
1
5
116
1
1
6
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Jan
J
a
n
115
1
1
5
116
1
1
6
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Feb
F
e
b
116
1
1
6
116
1
1
6
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Mar
M
a
r
115
1
1
5
115
1
1
5
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
Apr
A
p
r
114
1
1
4
114
1
1
4
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
May
M
a
y
113
1
1
3
112
1
1
2
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
Jun
J
u
n
112
1
1
2
111
1
1
1
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
Jul
J
u
l
111
1
1
1
110
1
1
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
Aug
A
u
g
110
1
1
0
108
1
0
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Sep
S
e
p
109
1
0
9
107
1
0
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Oct
O
c
t
108
1
0
8
106
1
0
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Nov
N
o
v
107
1
0
7
105
1
0
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Dec
D
e
c
106
1
0
6
103
1
0
3
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Jan
J
a
n
105
1
0
5
102
1
0
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Feb
F
e
b
104
1
0
4
101
1
0
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Mar
M
a
r
103
1
0
3
100
1
0
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Apr
A
p
r
100
1
0
0
97
9
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
May
M
a
y
100
1
0
0
97
9
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Jun
J
u
n
99
9
9
96
9
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
98
9
8
95
9
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
97
9
7
94
9
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
2029
2
0
2
9
2030
2
0
3
0
2031
2
0
3
1
Sep
S
e
p
96
9
6
93
9
3
0,0
0
,
0
0,0
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,
0
0,1
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1
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,
3
Oct
O
c
t
94
9
4
91
9
1
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0
,
0
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,
0
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1
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,
3
Nov
N
o
v
93
9
3
90
9
0
0,0
0
,
0
0,0
0
,
0
0,1
0
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1
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3
Dec
D
e
c
92
9
2
89
8
9
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,
0
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0
,
0
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1
0,3
0
,
3
Jan
J
a
n
92
9
2
88
8
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Feb
F
e
b
91
9
1
87
8
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Mar
M
a
r
90
9
0
86
8
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Apr
A
p
r
89
8
9
85
8
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
May
M
a
y
88
8
8
84
8
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jun
J
u
n
88
8
8
83
8
3
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
86
8
6
81
8
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
86
8
6
81
8
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
85
8
5
80
8
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
84
8
4
79
7
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
84
8
4
79
7
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
85
8
5
79
7
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jan
J
a
n
85
8
5
79
7
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Feb
F
e
b
85
8
5
79
7
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Mar
M
a
r
84
8
4
78
7
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Apr
A
p
r
83
8
3
77
7
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
May
M
a
y
82
8
2
76
7
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jun
J
u
n
80
8
0
75
7
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
79
7
9
74
7
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
78
7
8
72
7
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
77
7
7
71
7
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
76
7
6
70
7
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
75
7
5
69
6
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
74
7
4
68
6
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jan
J
a
n
73
7
3
66
6
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Feb
F
e
b
72
7
2
65
6
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Mar
M
a
r
71
7
1
64
6
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Apr
A
p
r
70
7
0
63
6
3
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
May
M
a
y
69
6
9
62
6
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jun
J
u
n
68
6
8
61
6
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
67
6
7
60
6
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
67
6
7
59
5
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
66
6
6
58
5
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
65
6
5
57
5
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
64
6
4
56
5
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
63
6
3
55
5
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Table
T
a
b
l
e
10
1
0
–
–
Production
P
r
o
d
u
c
t
i
o
n
Profile
P
r
o
f
i
l
e
data
d
a
t
a
(Constrained
(
C
o
n
s
t
r
a
i
n
e
d
Case)
C
a
s
e
)
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
-
-
Unconstrained
U
n
c
o
n
s
t
r
a
i
n
e
d
case
c
a
s
e
(max
(
m
a
x
trunkline
t
r
u
n
k
l
i
n
e
flowrate
f
l
o
w
r
a
t
e
270
2
7
0
MMSCFD)
M
M
S
C
F
D
)
Well
W
e
l
l
Gas
G
a
s
Rate
R
a
t
e
(MMSCFD)
(
M
M
S
C
F
D
)
Well
W
e
l
l
Cond
C
o
n
d
Rate
R
a
t
e
(STBD)
(
S
T
B
D
)
Well
W
e
l
l
Water
W
a
t
e
r
Rate
R
a
t
e
(STBD)
(
S
T
B
D
)
Year
Y
e
a
r
Month
M
o
n
t
h
-3
-
3
-4
-
4
-3
-
3
-4
-
4
-3
-
3
-4
-
4
2026
2
0
2
6
2027
2
0
2
7
2028
2
0
2
8
Jan
J
a
n
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Feb
F
e
b
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Mar
M
a
r
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Apr
A
p
r
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
May
M
a
y
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Jun
J
u
n
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Jul
J
u
l
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Aug
A
u
g
6
6
6
6
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Sep
S
e
p
108
1
0
8
108
1
0
8
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Oct
O
c
t
107
1
0
7
107
1
0
7
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Nov
N
o
v
110
1
1
0
111
1
1
1
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Dec
D
e
c
115
1
1
5
116
1
1
6
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Jan
J
a
n
119
1
1
9
120
1
2
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
Feb
F
e
b
122
1
2
2
122
1
2
2
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
Mar
M
a
r
125
1
2
5
125
1
2
5
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
Apr
A
p
r
129
1
2
9
128
1
2
8
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,2
0
,
2
May
M
a
y
133
1
3
3
132
1
3
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,2
0
,
2
Jun
J
u
n
131
1
3
1
130
1
3
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
129
1
2
9
127
1
2
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
126
1
2
6
124
1
2
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
124
1
2
4
122
1
2
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
122
1
2
2
120
1
2
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
120
1
2
0
117
1
1
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
118
1
1
8
115
1
1
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jan
J
a
n
116
1
1
6
113
1
1
3
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Feb
F
e
b
114
1
1
4
111
1
1
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Mar
M
a
r
112
1
1
2
109
1
0
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Apr
A
p
r
111
1
1
1
107
1
0
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
May
M
a
y
109
1
0
9
106
1
0
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jun
J
u
n
107
1
0
7
104
1
0
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
106
1
0
6
102
1
0
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
104
1
0
4
100
1
0
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
103
1
0
3
99
9
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
101
1
0
1
97
9
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
100
1
0
0
95
9
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
98
9
8
94
9
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
2029
2
0
2
9
2030
2
0
3
0
2031
2
0
3
1
Jan
J
a
n
97
9
7
92
9
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Feb
F
e
b
96
9
6
91
9
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Mar
M
a
r
96
9
6
91
9
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Apr
A
p
r
94
9
4
90
9
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
May
M
a
y
93
9
3
88
8
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jun
J
u
n
92
9
2
87
8
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
90
9
0
85
8
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
89
8
9
84
8
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
88
8
8
83
8
3
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
87
8
7
82
8
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
86
8
6
81
8
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
84
8
4
80
8
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jan
J
a
n
83
8
3
79
7
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Feb
F
e
b
82
8
2
77
7
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Mar
M
a
r
81
8
1
76
7
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Apr
A
p
r
80
8
0
75
7
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
May
M
a
y
79
7
9
74
7
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jun
J
u
n
78
7
8
73
7
3
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
77
7
7
72
7
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
76
7
6
70
7
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
75
7
5
69
6
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
74
7
4
68
6
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
73
7
3
67
6
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
72
7
2
66
6
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jan
J
a
n
71
7
1
65
6
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Feb
F
e
b
70
7
0
64
6
4
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Mar
M
a
r
69
6
9
63
6
3
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Apr
A
p
r
69
6
9
62
6
2
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
May
M
a
y
68
6
8
61
6
1
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jun
J
u
n
67
6
7
60
6
0
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Jul
J
u
l
66
6
6
59
5
9
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Aug
A
u
g
65
6
5
58
5
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Sep
S
e
p
65
6
5
58
5
8
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Oct
O
c
t
64
6
4
57
5
7
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Nov
N
o
v
63
6
3
56
5
6
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
62
6
2
55
5
5
0,0
0
,
0
0,0
0
,
0
0,1
0
,
1
0,3
0
,
3
Dec
D
e
c
0
0
0
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
0,0
0
,
0
Table
T
a
b
l
e
11
1
1
–
–
Production
P
r
o
d
u
c
t
i
o
n
Profile
P
r
o
f
i
l
e
data
d
a
t
a
(Unconstrained
(
U
n
c
o
n
s
t
r
a
i
n
e
d
Case)
C
a
s
e
)
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
8
8
DRILLING
D
R
I
L
L
I
N
G
&
&
COMPLETIONS
C
O
M
P
L
E
T
I
O
N
S
8.1
8
.
1
Drilling
D
r
i
l
l
i
n
g
and
a
n
d
Completions
C
o
m
p
l
e
t
i
o
n
s
overview
o
v
e
r
v
i
e
w
development
d
e
v
e
l
o
p
m
e
n
t
considers
c
o
n
s
i
d
e
r
s
the
t
h
e
drilling
d
r
i
l
l
i
n
g
of
o
f
two
t
w
o
wells:
w
e
l
l
s
:
Ø
Ø
-3
-
3
Ø
Ø
-4
-
4
8.2
8
.
2
Wells
W
e
l
l
s
targets
t
a
r
g
e
t
s
coordinates
c
o
o
r
d
i
n
a
t
e
s
The
T
h
e
following
f
o
l
l
o
w
i
n
g
table
t
a
b
l
e
resumes
r
e
s
u
m
e
s
the
t
h
e
preliminary
p
r
e
l
i
m
i
n
a
r
y
Wellheads
W
e
l
l
h
e
a
d
s
coordinates
c
o
o
r
d
i
n
a
t
e
s
as
a
s
per
p
e
r
[18].
[
1
8
]
.
Ø
Ø
PROJECT-3
P
R
O
J
E
C
T
-
3
Water
W
a
t
e
r
depth
d
e
p
t
h
RKB
R
K
B
elevation
e
l
e
v
a
t
i
o
n
Sea
S
e
a
Bed
B
e
d
(from
(
f
r
o
m
RKB)
R
K
B
)
(m)
(
m
)
(m)
(
m
)
(m)
(
m
)
811
8
1
1
25
2
5
836
8
3
6
Well
W
e
l
l
Head
H
e
a
d
coordinates
c
o
o
r
d
i
n
a
t
e
s
(Indonesia
(
I
n
d
o
n
e
s
i
a
Offshore
O
f
f
s
h
o
r
e
–
–
PROJECT-3
P
R
O
J
E
C
T
-
3
Expl.
E
x
p
l
.
Case
C
a
s
e
“b”)
“
b
”
)
Northing
N
o
r
t
h
i
n
g
(m)
(
m
)
South:
S
o
u
t
h
:
9,852,056
9
,
8
5
2
,
0
5
6
Easting
E
a
s
t
i
n
g
(m)
(
m
)
East:
E
a
s
t
:
583,427
5
8
3
,
4
2
7
Latitude
L
a
t
i
t
u
d
e
(y):
(
y
)
:
1°
1
°
20'
2
0
'
18.163"
1
8
.
1
6
3
"
S
S
Longitude
L
o
n
g
i
t
u
d
e
(x):
(
x
)
:
117°
1
1
7
°
44'
4
4
'
59.719"
5
9
.
7
1
9
"
E
E
Geodetic
G
e
o
d
e
t
i
c
System:
S
y
s
t
e
m
:
Universal
U
n
i
v
e
r
s
a
l
Transverse
T
r
a
n
s
v
e
r
s
e
Mercator
M
e
r
c
a
t
o
r
Geodetic
G
e
o
d
e
t
i
c
Datum:
D
a
t
u
m
:
WGS
W
G
S
1984
1
9
8
4
MAP
M
A
P
Zone:
Z
o
n
e
:
Zone
Z
o
n
e
50
5
0
S
S
(114
(
1
1
4
E
E
to
t
o
120
1
2
0
E)
E
)
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Ø
Ø
PROJECT-4
P
R
O
J
E
C
T
-
4
Water
W
a
t
e
r
depth
d
e
p
t
h
RKB
R
K
B
elevation
e
l
e
v
a
t
i
o
n
Sea
S
e
a
Bed
B
e
d
(from
(
f
r
o
m
RKB)
R
K
B
)
(m)
(
m
)
(m)
(
m
)
(m)
(
m
)
1103
1
1
0
3
29
2
9
1128
1
1
2
8
Well
W
e
l
l
Head
H
e
a
d
coordinates
c
o
o
r
d
i
n
a
t
e
s
(Indonesia
(
I
n
d
o
n
e
s
i
a
Offshore
O
f
f
s
h
o
r
e
-
-
-4)
-
4
)
Northing
N
o
r
t
h
i
n
g
(m)
(
m
)
South:
S
o
u
t
h
:
9,851,286
9
,
8
5
1
,
2
8
6
Easting
E
a
s
t
i
n
g
(m)
(
m
)
East:
E
a
s
t
:
585,820
5
8
5
,
8
2
0
Latitude
L
a
t
i
t
u
d
e
(y):
(
y
)
:
1°
1
°
20'
2
0
'
43.223"
4
3
.
2
2
3
"
S
S
Longitude
L
o
n
g
i
t
u
d
e
(x):
(
x
)
:
117°
1
1
7
°
46'
4
6
'
17.159"
1
7
.
1
5
9
"
E
E
Geodetic
G
e
o
d
e
t
i
c
System:
S
y
s
t
e
m
:
Universal
U
n
i
v
e
r
s
a
l
Transverse
T
r
a
n
s
v
e
r
s
e
Mercator
M
e
r
c
a
t
o
r
Geodetic
G
e
o
d
e
t
i
c
Datum:
D
a
t
u
m
:
WGS
W
G
S
1984
1
9
8
4
MAP
M
A
P
Zone:
Z
o
n
e
:
Zone
Z
o
n
e
50
5
0
S
S
(114
(
1
1
4
E
E
to
t
o
120
1
2
0
E)
E
)
8.3
8
.
3
Preliminary
P
r
e
l
i
m
i
n
a
r
y
Casing
C
a
s
i
n
g
Design
D
e
s
i
g
n
A
A
preliminary
p
r
e
l
i
m
i
n
a
r
y
material
m
a
t
e
r
i
a
l
selection,
s
e
l
e
c
t
i
o
n
,
considering
c
o
n
s
i
d
e
r
i
n
g
that
t
h
a
t
a
a
pore
p
o
r
e
pressure
p
r
e
s
s
u
r
e
study
s
t
u
d
y
is
i
s
not
n
o
t
still
s
t
i
l
l
available,
a
v
a
i
l
a
b
l
e
,
we
w
e
can
c
a
n
chose
c
h
o
s
e
like
l
i
k
e
casing
c
a
s
i
n
g
/
/
liner
l
i
n
e
r
string
s
t
r
i
n
g
the
t
h
e
same
s
a
m
e
material
m
a
t
e
r
i
a
l
and
a
n
d
size
s
i
z
e
already
a
l
r
e
a
d
y
used
u
s
e
d
for
f
o
r
Merakes
M
e
r
a
k
e
s
&
&
Jangkrik
J
a
n
g
k
r
i
k
projects
p
r
o
j
e
c
t
s
and
a
n
d
to
t
o
consider
c
o
n
s
i
d
e
r
what
w
h
a
t
has
h
a
s
been
b
e
e
n
already
a
l
r
e
a
d
y
“planned
“
p
l
a
n
n
e
d
/
/
mentioned”
m
e
n
t
i
o
n
e
d
”
within
w
i
t
h
i
n
Gas
G
a
s
Brand
B
r
a
n
d
IDD
I
D
D
(Indonesia
(
I
n
d
o
n
e
s
i
a
Deepwater
D
e
e
p
w
a
t
e
r
Development)
D
e
v
e
l
o
p
m
e
n
t
)
Project,
P
r
o
j
e
c
t
,
POD
P
O
D
June
J
u
n
e
2018.
2
0
1
8
.
Size
S
i
z
e
(Inches)
(
I
n
c
h
e
s
)
Steel
S
t
e
e
l
grade
g
r
a
d
e
(
(
//
/
/
)
)
Wall
W
a
l
l
thikness
t
h
i
k
n
e
s
s
(Inches)
(
I
n
c
h
e
s
)
CASING
C
A
S
I
N
G
SETTING
S
E
T
T
I
N
G
DEPTH
D
E
P
T
H
"PROJECT-3"
"
P
R
O
J
E
C
T
-
3
"
(proposed).
(
p
r
o
p
o
s
e
d
)
.
Weight
W
e
i
g
h
t
(Lb/ft)
(
L
b
/
f
t
)
Connection
C
o
n
n
e
c
t
i
o
n
type
t
y
p
e
(
(
//
/
/
)
)
Csg
C
s
g
shoe
s
h
o
e
depth
d
e
p
t
h
(TVDss)
(
T
V
D
s
s
)
(m)
(
m
)
Csg
C
s
g
shoe
s
h
o
e
depth
d
e
p
t
h
(TVD)
(
T
V
D
)
(m)
(
m
)
Csg
C
s
g
shoe
s
h
o
e
depth
d
e
p
t
h
(MD)
(
M
D
)
(m)
(
m
)
Csg
C
s
g
/
/
Liner
L
i
n
e
r
Lenght
L
e
n
g
h
t
(MD)
(
M
D
)
(m)
(
m
)
Quick
Q
u
i
c
k
36
3
6
X52
X
5
2
1,5
1
,
5
552,7
5
5
2
,
7
881
8
8
1
906
9
0
6
906
9
0
6
70
7
0
Connector
C
o
n
n
e
c
t
o
r
Quick
Q
u
i
c
k
20
2
0
X56
X
5
6
0,812
0
,
8
1
2
166,4
1
6
6
,
4
Connector
C
o
n
n
e
c
t
o
r
1461
1
4
6
1
1486
1
4
8
6
1486
1
4
8
6
650
6
5
0
13,625
1
3
,
6
2
5
P110
P
1
1
0
0,625
0
,
6
2
5
88,2
8
8
,
2
Premium
P
r
e
m
i
u
m
2075
2
0
7
5
2100
2
1
0
0
2171
2
1
7
1
1335
1
3
3
5
10,75
1
0
,
7
5
T95/P110
T
9
5
/
P
1
1
0
0.595
0
.
5
9
5
65.7
6
5
.
7
Premium
P
r
e
m
i
u
m
2674
2
6
7
4
2699
2
6
9
9
3178
3
1
7
8
1127
1
1
2
7
10-3/4
1
0
-
3
/
4
Liner
L
i
n
e
r
TOL
T
O
L
(TVDss):
(
T
V
D
s
s
)
:
1989m
1
9
8
9
m
TOL
T
O
L
(TVD):
(
T
V
D
)
:
2014m
2
0
1
4
m
TOL
T
O
L
(MD):
(
M
D
)
:
2051m
2
0
5
1
m
-3
-
3
Csg
C
s
g
/Lnr
/
L
n
r
setting
s
e
t
t
i
n
g
depth
d
e
p
t
h
&
&
Type
T
y
p
e
Total
T
o
t
a
l
liner
l
i
n
e
r
length:
l
e
n
g
t
h
:
1127m
1
1
2
7
m
MD
M
D
Liner
L
i
n
e
r
Overlap:
O
v
e
r
l
a
p
:
120m
1
2
0
m
MD
M
D
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Size
S
i
z
e
(Inches)
(
I
n
c
h
e
s
)
Steel
S
t
e
e
l
grade
g
r
a
d
e
(
(
//
/
/
)
)
Wall
W
a
l
l
thikness
t
h
i
k
n
e
s
s
(Inches)
(
I
n
c
h
e
s
)
CASING
C
A
S
I
N
G
SETTING
S
E
T
T
I
N
G
DEPTH
D
E
P
T
H
"PROJECT-4"
"
P
R
O
J
E
C
T
-
4
"
(proposed).
(
p
r
o
p
o
s
e
d
)
.
Weight
W
e
i
g
h
t
(Lb/ft)
(
L
b
/
f
t
)
36
3
6
X52
X
5
2
1,5
1
,
5
552,7
5
5
2
,
7
20
2
0
X56
X
5
6
0,812
0
,
8
1
2
166,4
1
6
6
,
4
Connectio
C
o
n
n
e
c
t
i
o
n
n
type
t
y
p
e
(
(
//
/
/
)
)
Quick
Q
u
i
c
k
Connector
C
o
n
n
e
c
t
o
r
Quick
Q
u
i
c
k
Connector
C
o
n
n
e
c
t
o
r
Csg
C
s
g
shoe
s
h
o
e
depth
d
e
p
t
h
(TVDss)
(
T
V
D
s
s
)
(m)
(
m
)
Csg
C
s
g
shoe
s
h
o
e
depth
d
e
p
t
h
(TVD)
(
T
V
D
)
(m)
(
m
)
Csg
C
s
g
shoe
s
h
o
e
depth
d
e
p
t
h
(MD)
(
M
D
)
(m)
(
m
)
Casing
C
a
s
i
n
g
/
/
Liner
L
i
n
e
r
Lenght
L
e
n
g
h
t
(MD)
(
M
D
)
(m)
(
m
)
1173.48
1
1
7
3
.
4
8
1198
1
1
9
8
1198
1
1
9
8
70
7
0
1703.48
1
7
0
3
.
4
8
1728
1
7
2
8
1728
1
7
2
8
600
6
0
0
13,625
1
3
,
6
2
5
P110
P
1
1
0
0,625
0
,
6
2
5
88,2
8
8
,
2
Premium
P
r
e
m
i
u
m
2225
2
2
2
5
2250
2
2
5
0
2272
2
2
7
2
1144
1
1
4
4
10,75
1
0
,
7
5
T95/P110
T
9
5
/
P
1
1
0
0.595
0
.
5
9
5
53,5
5
3
,
5
Premium
P
r
e
m
i
u
m
2844
2
8
4
4
2869
2
8
6
9
3302
3
3
0
2
1150
1
1
5
0
7
7
P110
P
1
1
0
0,453
0
,
4
5
3
32
3
2
Premium
P
r
e
m
i
u
m
3353
3
3
5
3
3378
3
3
7
8
4205
4
2
0
5
1023
1
0
2
3
Note:
N
o
t
e
:
The
T
h
e
contingency
c
o
n
t
i
n
g
e
n
c
y
of
o
f
7”
7
”
Liner
L
i
n
e
r
will
w
i
l
l
be
b
e
set
s
e
t
only
o
n
l
y
to
t
o
cover
c
o
v
e
r
exploration
e
x
p
l
o
r
a
t
i
o
n
tail
t
a
i
l
incase
i
n
c
a
s
e
needed.
n
e
e
d
e
d
.
10-3/4
1
0
-
3
/
4
Liner
L
i
n
e
r
TOL
T
O
L
(TVDss):
(
T
V
D
s
s
)
:
2120m
2
1
2
0
m
TOL
T
O
L
(TVD):
(
T
V
D
)
:
2145m
2
1
4
5
m
TOL
T
O
L
(MD):
(
M
D
)
:
2152m
2
1
5
2
m
Total
T
o
t
a
l
liner
l
i
n
e
r
length:
l
e
n
g
t
h
:
1150m
1
1
5
0
m
MD
M
D
Liner
L
i
n
e
r
Overlap:
O
v
e
r
l
a
p
:
120m
1
2
0
m
MD
M
D
7
7
Liner
L
i
n
e
r
TOL
T
O
L
(TVDss):
(
T
V
D
s
s
)
:
2777m
2
7
7
7
m
TOL
T
O
L
(TVD):
(
T
V
D
)
:
2802m
2
8
0
2
m
TOL
T
O
L
(MD):
(
M
D
)
:
3182m
3
1
8
2
m
-4
-
4
Csg
C
s
g
/Lnr
/
L
n
r
setting
s
e
t
t
i
n
g
depth
d
e
p
t
h
&
&
Type
T
y
p
e
Total
T
o
t
a
l
liner
l
i
n
e
r
length:
l
e
n
g
t
h
:
1023m
1
0
2
3
m
MD
M
D
Liner
L
i
n
e
r
Overlap:
O
v
e
r
l
a
p
:
120m
1
2
0
m
MD
M
D
Based
B
a
s
e
d
on
o
n
experience,
e
x
p
e
r
i
e
n
c
e
,
no
n
o
H2S
H
2
S
is
i
s
not
n
o
t
present
p
r
e
s
e
n
t
in
i
n
the
t
h
e
field.
f
i
e
l
d
.
Fluid
F
l
u
i
d
sampling
s
a
m
p
l
i
n
g
was
w
a
s
obtained
o
b
t
a
i
n
e
d
using
u
s
i
n
g
the
t
h
e
MDT
M
D
T
tool
t
o
o
l
in
i
n
both
b
o
t
h
the
t
h
e
Gendalo-4
G
e
n
d
a
l
o
-
4
and
a
n
d
-1
-
1
wellbores.
w
e
l
l
b
o
r
e
s
.
All
A
l
l
samples
s
a
m
p
l
e
s
obtained
o
b
t
a
i
n
e
d
using
u
s
i
n
g
the
t
h
e
MDT
M
D
T
tool
t
o
o
l
were
w
e
r
e
contaminated
c
o
n
t
a
m
i
n
a
t
e
d
with
w
i
t
h
synthetic
s
y
n
t
h
e
t
i
c
oil-based
o
i
l
-
b
a
s
e
d
drilling
d
r
i
l
l
i
n
g
fluids,
f
l
u
i
d
s
,
resulting
r
e
s
u
l
t
i
n
g
in
i
n
questionable
q
u
e
s
t
i
o
n
a
b
l
e
measurements
m
e
a
s
u
r
e
m
e
n
t
s
of
o
f
condensate
c
o
n
d
e
n
s
a
t
e
yield.
y
i
e
l
d
.
Since
S
i
n
c
e
there
t
h
e
r
e
are
a
r
e
no
n
o
specific
s
p
e
c
i
f
i
c
lab
l
a
b
analysis
a
n
a
l
y
s
i
s
reports
r
e
p
o
r
t
s
of
o
f
the
t
h
e
MDT
M
D
T
samples
s
a
m
p
l
e
s
collected
c
o
l
l
e
c
t
e
d
for
f
o
r
the
t
h
e
secondary
s
e
c
o
n
d
a
r
y
reservoirs
r
e
s
e
r
v
o
i
r
s
in
i
n
(3140/50
(
3
1
4
0
/
5
0
&
&
3170),
3
1
7
0
)
,
the
t
h
e
3130
3
1
3
0
fluid
f
l
u
i
d
properties
p
r
o
p
e
r
t
i
e
s
can
c
a
n
be
b
e
assumed
a
s
s
u
m
e
d
for
f
o
r
the
t
h
e
secondary
s
e
c
o
n
d
a
r
y
reservoirs.
r
e
s
e
r
v
o
i
r
s
.
The
T
h
e
properties
p
r
o
p
e
r
t
i
e
s
from
f
r
o
m
sample
s
a
m
p
l
e
#
#
JFL2002074
J
F
L
2
0
0
2
0
7
4
are
a
r
e
shown
s
h
o
w
n
in
i
n
table
t
a
b
l
e
below.
b
e
l
o
w
.
In
I
n
order
o
r
d
e
r
to
t
o
estimate
e
s
t
i
m
a
t
e
condensate
c
o
n
d
e
n
s
a
t
e
yield,
y
i
e
l
d
,
the
t
h
e
observed
o
b
s
e
r
v
e
d
MDT
M
D
T
pressure
p
r
e
s
s
u
r
e
gradient
g
r
a
d
i
e
n
t
in
i
n
the
t
h
e
3140/50
3
1
4
0
/
5
0
was
w
a
s
matched
m
a
t
c
h
e
d
using
u
s
i
n
g
a
a
fluid
f
l
u
i
d
density
d
e
n
s
i
t
y
calculation.
c
a
l
c
u
l
a
t
i
o
n
.
The
T
h
e
technique
t
e
c
h
n
i
q
u
e
was
w
a
s
found
f
o
u
n
d
not
n
o
t
to
t
o
be
b
e
sensitive
s
e
n
s
i
t
i
v
e
to
t
o
condensate
c
o
n
d
e
n
s
a
t
e
gravity
g
r
a
v
i
t
y
and
a
n
d
results
r
e
s
u
l
t
s
in
i
n
condensate
c
o
n
d
e
n
s
a
t
e
yield
y
i
e
l
d
estimation
e
s
t
i
m
a
t
i
o
n
of
o
f
2
2
bbl
b
b
l
/
/
mmcf.
m
m
c
f
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
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On
O
n
-1
-
1
fluid
f
l
u
i
d
samples
s
a
m
p
l
e
s
indicate
i
n
d
i
c
a
t
e
the
t
h
e
need
n
e
e
d
for
f
o
r
corrosion
c
o
r
r
o
s
i
o
n
resistant
r
e
s
i
s
t
a
n
t
alloys
a
l
l
o
y
s
in
i
n
the
t
h
e
flow-wetted
f
l
o
w
-
w
e
t
t
e
d
tubulars.
t
u
b
u
l
a
r
s
.
Main
M
a
i
n
contributor
c
o
n
t
r
i
b
u
t
o
r
on
o
n
corrosion
c
o
r
r
o
s
i
o
n
potential
p
o
t
e
n
t
i
a
l
on
o
n
field
f
i
e
l
d
was
w
a
s
CO2
C
O
2
in
i
n
formation.
f
o
r
m
a
t
i
o
n
.
High
H
i
g
h
partial
p
a
r
t
i
a
l
pressure
p
r
e
s
s
u
r
e
value
v
a
l
u
e
shows
s
h
o
w
s
the
t
h
e
requirement
r
e
q
u
i
r
e
m
e
n
t
of
o
f
corrosive
c
o
r
r
o
s
i
v
e
resistance
r
e
s
i
s
t
a
n
c
e
material
m
a
t
e
r
i
a
l
on
o
n
flow
f
l
o
w
wetted
w
e
t
t
e
d
including
i
n
c
l
u
d
i
n
g
9
9
⅝”
⅝
”
production
p
r
o
d
u
c
t
i
o
n
liner
l
i
n
e
r
and
a
n
d
5
5
½“
½
“
production
p
r
o
d
u
c
t
i
o
n
tubing.
t
u
b
i
n
g
.
The
T
h
e
use
u
s
e
of
o
f
13
1
3
Cr
C
r
(or
(
o
r
Super
S
u
p
e
r
13
1
3
Cr)
C
r
)
martensitic
m
a
r
t
e
n
s
i
t
i
c
stainless
s
t
a
i
n
l
e
s
s
steel
s
t
e
e
l
could
c
o
u
l
d
be
b
e
a
a
solution
s
o
l
u
t
i
o
n
to
t
o
prevent
p
r
e
v
e
n
t
the
t
h
e
corrosion
c
o
r
r
o
s
i
o
n
phenomenon.
p
h
e
n
o
m
e
n
o
n
.
For
F
o
r
the
t
h
e
casing
c
a
s
i
n
g
above
a
b
o
v
e
packer
p
a
c
k
e
r
carbon
c
a
r
b
o
n
or
o
r
low
l
o
w
alloy
a
l
l
o
y
steel
s
t
e
e
l
material
m
a
t
e
r
i
a
l
is
i
s
a
a
suitable.
s
u
i
t
a
b
l
e
.
It
I
t
can
c
a
n
be
b
e
selected
s
e
l
e
c
t
e
d
among
a
m
o
n
g
sour
s
o
u
r
service
s
e
r
v
i
c
e
materials,
m
a
t
e
r
i
a
l
s
,
according
a
c
c
o
r
d
i
n
g
to
t
o
mechanical
m
e
c
h
a
n
i
c
a
l
strength
s
t
r
e
n
g
t
h
required
r
e
q
u
i
r
e
d
for
f
o
r
the
t
h
e
casing
c
a
s
i
n
g
application
a
p
p
l
i
c
a
t
i
o
n
according
a
c
c
o
r
d
i
n
g
to
t
o
API
A
P
I
5CT.
5
C
T
.
8.4
8
.
4
Completion
C
o
m
p
l
e
t
i
o
n
Schematics
S
c
h
e
m
a
t
i
c
s
The
T
h
e
design
d
e
s
i
g
n
has
h
a
s
been
b
e
e
n
prepared
p
r
e
p
a
r
e
d
in
i
n
compliance
c
o
m
p
l
i
a
n
c
e
with
w
i
t
h
“Completion
“
C
o
m
p
l
e
t
i
o
n
Design
D
e
s
i
g
n
Procedure”
P
r
o
c
e
d
u
r
e
”
(STAP-P-
(
S
T
A
P
-
P
-
1-
1
-
M-26543).
M
-
2
6
5
4
3
)
.
The
T
h
e
following
f
o
l
l
o
w
i
n
g
considerations
c
o
n
s
i
d
e
r
a
t
i
o
n
s
have
h
a
v
e
been
b
e
e
n
taken
t
a
k
e
n
into
i
n
t
o
account
a
c
c
o
u
n
t
in
i
n
the
t
h
e
current
c
u
r
r
e
n
t
completion
c
o
m
p
l
e
t
i
o
n
design:
d
e
s
i
g
n
:
-
-
Respect
R
e
s
p
e
c
t
of
o
f
HSE
H
S
E
regulations.
r
e
g
u
l
a
t
i
o
n
s
.
-
-
Capability
C
a
p
a
b
i
l
i
t
y
to
t
o
deliver
d
e
l
i
v
e
r
forecasted
f
o
r
e
c
a
s
t
e
d
hydrocarbon
h
y
d
r
o
c
a
r
b
o
n
production
p
r
o
d
u
c
t
i
o
n
rates.
r
a
t
e
s
.
-
-
Capability
C
a
p
a
b
i
l
i
t
y
to
t
o
inject
i
n
j
e
c
t
adequate
a
d
e
q
u
a
t
e
water
w
a
t
e
r
and
a
n
d
gas
g
a
s
rates.
r
a
t
e
s
.
-
-
Safety
S
a
f
e
t
y
of
o
f
operations
o
p
e
r
a
t
i
o
n
s
and
a
n
d
reliability
r
e
l
i
a
b
i
l
i
t
y
of
o
f
equipment.
e
q
u
i
p
m
e
n
t
.
-
-
Longevity
L
o
n
g
e
v
i
t
y
for
f
o
r
the
t
h
e
full
f
u
l
l
wells
w
e
l
l
s
lifetime.
l
i
f
e
t
i
m
e
.
-
-
Operational
O
p
e
r
a
t
i
o
n
a
l
time
t
i
m
e
optimization
o
p
t
i
m
i
z
a
t
i
o
n
due
d
u
e
to
t
o
high
h
i
g
h
daily
d
a
i
l
y
rig
r
i
g
cost.
c
o
s
t
.
-
-
Simplicity
S
i
m
p
l
i
c
i
t
y
of
o
f
design
d
e
s
i
g
n
with
w
i
t
h
standard
s
t
a
n
d
a
r
d
and
a
n
d
field
f
i
e
l
d
proven
p
r
o
v
e
n
technology.
t
e
c
h
n
o
l
o
g
y
.
-
-
Equipment
E
q
u
i
p
m
e
n
t
cost
c
o
s
t
and
a
n
d
delivery
d
e
l
i
v
e
r
y
time
t
i
m
e
reduction
r
e
d
u
c
t
i
o
n
achieved
a
c
h
i
e
v
e
d
by
b
y
standardization.
s
t
a
n
d
a
r
d
i
z
a
t
i
o
n
.
-
-
Capability
C
a
p
a
b
i
l
i
t
y
to
t
o
cope
c
o
p
e
with
w
i
t
h
the
t
h
e
worst
w
o
r
s
t
anticipated
a
n
t
i
c
i
p
a
t
e
d
operating
o
p
e
r
a
t
i
n
g
loads
l
o
a
d
s
and
a
n
d
environment.
e
n
v
i
r
o
n
m
e
n
t
.
-
-
In
I
n
compliance
c
o
m
p
l
i
a
n
c
e
with
w
i
t
h
International
I
n
t
e
r
n
a
t
i
o
n
a
l
Standards
S
t
a
n
d
a
r
d
s
and
a
n
d
good
g
o
o
d
oilfield
o
i
l
f
i
e
l
d
practices.
p
r
a
c
t
i
c
e
s
.
Three
T
h
r
e
e
well
w
e
l
l
completion
c
o
m
p
l
e
t
i
o
n
typologies
t
y
p
o
l
o
g
i
e
s
will
w
i
l
l
be
b
e
evaluated:
e
v
a
l
u
a
t
e
d
:
-
3
3
(scenario
(
s
c
e
n
a
r
i
o
4)
4
)
well
w
e
l
l
would
w
o
u
l
d
be
b
e
completed
c
o
m
p
l
e
t
e
d
in
i
n
two
t
w
o
production
p
r
o
d
u
c
t
i
o
n
zones
z
o
n
e
s
with
w
i
t
h
CHFP
C
H
F
P
in
i
n
10¾”
1
0
¾
”
liner
l
i
n
e
r
and
a
n
d
smart
s
m
a
r
t
upper
u
p
p
e
r
completion.
c
o
m
p
l
e
t
i
o
n
.
-
4
4
well
w
e
l
l
would
w
o
u
l
d
be
b
e
completed
c
o
m
p
l
e
t
e
d
with
w
i
t
h
1
1
CHFP
C
H
F
P
inside
i
n
s
i
d
e
10¾”
1
0
¾
”
liner
l
i
n
e
r
with
w
i
t
h
posibility
p
o
s
i
b
i
l
i
t
y
to
t
o
split
s
p
l
i
t
into
i
n
t
o
2
2
stack.
s
t
a
c
k
.
Upper
U
p
p
e
r
smart
s
m
a
r
t
completion
c
o
m
p
l
e
t
i
o
n
will
w
i
l
l
be
b
e
also
a
l
s
o
available
a
v
a
i
l
a
b
l
e
incase
i
n
c
a
s
e
required.
r
e
q
u
i
r
e
d
.
Current
C
u
r
r
e
n
t
completion
c
o
m
p
l
e
t
i
o
n
strategy
s
t
r
a
t
e
g
y
designed
d
e
s
i
g
n
e
d
to
t
o
maximize
m
a
x
i
m
i
z
e
well
w
e
l
l
deliverability
d
e
l
i
v
e
r
a
b
i
l
i
t
y
by
b
y
upsize
u
p
s
i
z
e
the
t
h
e
completion
c
o
m
p
l
e
t
i
o
n
size
s
i
z
e
to
t
o
allow
a
l
l
o
w
higher
h
i
g
h
e
r
gas
g
a
s
rate
r
a
t
e
in
i
n
10-3/4”
1
0
-
3
/
4
”
liner
l
i
n
e
r
system
s
y
s
t
e
m
compared
c
o
m
p
a
r
e
d
with
w
i
t
h
9-5/8”
9
-
5
/
8
”
liner
l
i
n
e
r
system.
s
y
s
t
e
m
.
Other
O
t
h
e
r
options
o
p
t
i
o
n
s
can
c
a
n
be
b
e
further
f
u
r
t
h
e
r
evaluated
e
v
a
l
u
a
t
e
d
at
a
t
later
l
a
t
e
r
stage
s
t
a
g
e
of
o
f
the
t
h
e
project.
p
r
o
j
e
c
t
.
8.5
8
.
5
Preliminary
P
r
e
l
i
m
i
n
a
r
y
Metallurgy
M
e
t
a
l
l
u
r
g
y
and
a
n
d
Elastomers
E
l
a
s
t
o
m
e
r
s
Selection
S
e
l
e
c
t
i
o
n
No
N
o
dedicated
d
e
d
i
c
a
t
e
d
completion
c
o
m
p
l
e
t
i
o
n
material
m
a
t
e
r
i
a
l
study
s
t
u
d
y
has
h
a
s
been
b
e
e
n
commissioned
c
o
m
m
i
s
s
i
o
n
e
d
yet.
y
e
t
.
However
H
o
w
e
v
e
r
13Cr
1
3
C
r
material
m
a
t
e
r
i
a
l
will
w
i
l
l
be
b
e
considered
c
o
n
s
i
d
e
r
e
d
as
a
s
most
m
o
s
t
likely
l
i
k
e
l
y
for
f
o
r
the
t
h
e
analogy
a
n
a
l
o
g
y
with
w
i
t
h
other
o
t
h
e
r
indonesian
i
n
d
o
n
e
s
i
a
n
project
p
r
o
j
e
c
t
already
a
l
r
e
a
d
y
developed
d
e
v
e
l
o
p
e
d
(Jangkrik,
(
J
a
n
g
k
r
i
k
,
Merakes).
M
e
r
a
k
e
s
)
.
This
T
h
i
s
consideration
c
o
n
s
i
d
e
r
a
t
i
o
n
will
w
i
l
l
be
b
e
apllied
a
p
l
l
i
e
d
also
a
l
s
o
for
f
o
r
cost
c
o
s
t
evaluation.
e
v
a
l
u
a
t
i
o
n
.
This
T
h
i
s
aspect
a
s
p
e
c
t
will
w
i
l
l
be
b
e
further
f
u
r
t
h
e
r
analized
a
n
a
l
i
z
e
d
in
i
n
the
t
h
e
followig
f
o
l
l
o
w
i
g
step
s
t
e
p
of
o
f
the
t
h
e
project.
p
r
o
j
e
c
t
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
9
9
FLUID
F
L
U
I
D
DATA
D
A
T
A
AND
A
N
D
PRODUCTION
P
R
O
D
U
C
T
I
O
N
CHEMISTRY
C
H
E
M
I
S
T
R
Y
9.1
9
.
1
Reservoir
R
e
s
e
r
v
o
i
r
Fluid
F
l
u
i
d
Properties
P
r
o
p
e
r
t
i
e
s
Due
D
u
e
to
t
o
expected
e
x
p
e
c
t
e
d
high
h
i
g
h
pressure
p
r
e
s
s
u
r
e
and
a
n
d
relatively
r
e
l
a
t
i
v
e
l
y
low
l
o
w
temperature
t
e
m
p
e
r
a
t
u
r
e
during
d
u
r
i
n
g
both
b
o
t
h
normal
n
o
r
m
a
l
and
a
n
d
transient
t
r
a
n
s
i
e
n
t
operations,
o
p
e
r
a
t
i
o
n
s
,
fluids
f
l
u
i
d
s
are
a
r
e
expected
e
x
p
e
c
t
e
d
to
t
o
be
b
e
susceptible
s
u
s
c
e
p
t
i
b
l
e
to
t
o
hydrate
h
y
d
r
a
t
e
formation.
f
o
r
m
a
t
i
o
n
.
Hydrates
H
y
d
r
a
t
e
s
formation
f
o
r
m
a
t
i
o
n
shall
s
h
a
l
l
be
b
e
avoided
a
v
o
i
d
e
d
in
i
n
all
a
l
l
scenarios
s
c
e
n
a
r
i
o
s
by
b
y
means
m
e
a
n
s
of
o
f
continuous
c
o
n
t
i
n
u
o
u
s
hydrates
h
y
d
r
a
t
e
s
inhibitor
i
n
h
i
b
i
t
o
r
injection
i
n
j
e
c
t
i
o
n
(Lean
(
L
e
a
n
MEG
M
E
G
solution
s
o
l
u
t
i
o
n
MEG
M
E
G
80%wt).
8
0
%
w
t
)
.
Similar
S
i
m
i
l
a
r
hydrate
h
y
d
r
a
t
e
prevention
p
r
e
v
e
n
t
i
o
n
strategy
s
t
r
a
t
e
g
y
as
a
s
for
f
o
r
JKK
J
K
K
and
a
n
d
Merakes
M
e
r
a
k
e
s
field
f
i
e
l
d
is
i
s
considered.
c
o
n
s
i
d
e
r
e
d
.
MeOH
M
e
O
H
is
i
s
injected
i
n
j
e
c
t
e
d
in
i
n
start-up
s
t
a
r
t
-
u
p
/
/
restart
r
e
s
t
a
r
t
due
d
u
e
to
t
o
avoid
a
v
o
i
d
low
l
o
w
temperature
t
e
m
p
e
r
a
t
u
r
e
issues
i
s
s
u
e
s
and
a
n
d
hydrate
h
y
d
r
a
t
e
formation
f
o
r
m
a
t
i
o
n
risks.
r
i
s
k
s
.
No
N
o
asphaltenes,
a
s
p
h
a
l
t
e
n
e
s
,
foaming
f
o
a
m
i
n
g
and
a
n
d
emulsion
e
m
u
l
s
i
o
n
formations
f
o
r
m
a
t
i
o
n
s
are
a
r
e
assumed
a
s
s
u
m
e
d
present
p
r
e
s
e
n
t
in
i
n
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluids.
f
l
u
i
d
s
.
Scale
S
c
a
l
e
formation
f
o
r
m
a
t
i
o
n
is
i
s
assumed
a
s
s
u
m
e
d
present
p
r
e
s
e
n
t
as
a
s
for
f
o
r
JKK
J
K
K
and
a
n
d
Merakes
M
e
r
a
k
e
s
reservoir
r
e
s
e
r
v
o
i
r
fluids.
f
l
u
i
d
s
.
9.2
9
.
2
Reservoir
R
e
s
e
r
v
o
i
r
Fluid
F
l
u
i
d
Composition
C
o
m
p
o
s
i
t
i
o
n
For
F
o
r
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid
f
l
u
i
d
composition,
c
o
m
p
o
s
i
t
i
o
n
,
ref.
r
e
f
.
to
t
o
7.2.
7
.
2
.
9.3
9
.
3
Scale
S
c
a
l
e
Potential
P
o
t
e
n
t
i
a
l
Scale
S
c
a
l
e
formation
f
o
r
m
a
t
i
o
n
is
i
s
assumed
a
s
s
u
m
e
d
present
p
r
e
s
e
n
t
as
a
s
for
f
o
r
JKK
J
K
K
and
a
n
d
Merakes
M
e
r
a
k
e
s
reservoir
r
e
s
e
r
v
o
i
r
fluids.
f
l
u
i
d
s
.
9.4
9
.
4
Wax
W
a
x
Formation
F
o
r
m
a
t
i
o
n
and
a
n
d
Rheology
R
h
e
o
l
o
g
y
See
S
e
e
9.1,
9
.
1
,
no
n
o
waxes,
w
a
x
e
s
,
foaming
f
o
a
m
i
n
g
and
a
n
d
emulsion
e
m
u
l
s
i
o
n
formations
f
o
r
m
a
t
i
o
n
s
are
a
r
e
expected
e
x
p
e
c
t
e
d
in
i
n
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid.
f
l
u
i
d
.
9.5
9
.
5
Hydrate
H
y
d
r
a
t
e
Equilibrium
E
q
u
i
l
i
b
r
i
u
m
Curves
C
u
r
v
e
s
Hydrates
H
y
d
r
a
t
e
s
curve
c
u
r
v
e
have
h
a
v
e
been
b
e
e
n
calculated
c
a
l
c
u
l
a
t
e
d
with
w
i
t
h
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid
f
l
u
i
d
composition
c
o
m
p
o
s
i
t
i
o
n
reported
r
e
p
o
r
t
e
d
in
i
n
section
s
e
c
t
i
o
n
7.2
7
.
2
saturated
s
a
t
u
r
a
t
e
d
at
a
t
reservoir
r
e
s
e
r
v
o
i
r
conditions
c
o
n
d
i
t
i
o
n
s
(30
(
3
0
bar,
b
a
r
,
74°C).
7
4
°
C
)
.
Figure
F
i
g
u
r
e
5:
5
:
-
-
Hydrate
H
y
d
r
a
t
e
formation
f
o
r
m
a
t
i
o
n
curves
c
u
r
v
e
s
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
9.6
9
.
6
Hydrogen
H
y
d
r
o
g
e
n
Sulphide
S
u
l
p
h
i
d
e
The
T
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid
f
l
u
i
d
is
i
s
expected
e
x
p
e
c
t
e
d
to
t
o
be
b
e
H2S
H
2
S
free.
f
r
e
e
.
9.7
9
.
7
Asphaltenes
A
s
p
h
a
l
t
e
n
e
s
No
N
o
asphaltenes
a
s
p
h
a
l
t
e
n
e
s
are
a
r
e
expected
e
x
p
e
c
t
e
d
in
i
n
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid.
f
l
u
i
d
.
9.8
9
.
8
Material
M
a
t
e
r
i
a
l
Selection
S
e
l
e
c
t
i
o
n
As
A
s
no
n
o
data
d
a
t
a
are
a
r
e
available
a
v
a
i
l
a
b
l
e
on
o
n
water
w
a
t
e
r
analysis,
a
n
a
l
y
s
i
s
,
the
t
h
e
same
s
a
m
e
chemical
c
h
e
m
i
c
a
l
composition
c
o
m
p
o
s
i
t
i
o
n
as
a
s
for
f
o
r
JKNE
J
K
N
E
will
w
i
l
l
be
b
e
considered
c
o
n
s
i
d
e
r
e
d
with
w
i
t
h
as
a
s
main
m
a
i
n
constituent
c
o
n
s
t
i
t
u
e
n
t
used
u
s
e
d
for
f
o
r
material
m
a
t
e
r
i
a
l
selection
s
e
l
e
c
t
i
o
n
carbonate
c
a
r
b
o
n
a
t
e
with
w
i
t
h
a
a
content
c
o
n
t
e
n
t
equal
e
q
u
a
l
to
t
o
105
1
0
5
meq/l.
m
e
q
/
l
.
9.8.1
9
.
8
.
1
CO2
C
O
2
Corrosion
C
o
r
r
o
s
i
o
n
Wet
W
e
t
CO2
C
O
2
corrosion
c
o
r
r
o
s
i
o
n
is
i
s
generally
g
e
n
e
r
a
l
l
y
referred
r
e
f
e
r
r
e
d
as
a
s
‘sweet
‘
s
w
e
e
t
corrosion’
c
o
r
r
o
s
i
o
n
’
when
w
h
e
n
H2S
H
2
S
is
i
s
absent.
a
b
s
e
n
t
.
When
W
h
e
n
CO2
C
O
2
is
i
s
present
p
r
e
s
e
n
t
in
i
n
the
t
h
e
gas
g
a
s
phase,
p
h
a
s
e
,
any
a
n
y
water
w
a
t
e
r
in
i
n
contact
c
o
n
t
a
c
t
with
w
i
t
h
this
t
h
i
s
gas
g
a
s
will
w
i
l
l
dissolve
d
i
s
s
o
l
v
e
CO2
C
O
2
to
t
o
a
a
concentration
c
o
n
c
e
n
t
r
a
t
i
o
n
proportional
p
r
o
p
o
r
t
i
o
n
a
l
to
t
o
the
t
h
e
partial
p
a
r
t
i
a
l
pressure
p
r
e
s
s
u
r
e
pCO2,
p
C
O
2
,
of
o
f
the
t
h
e
CO2
C
O
2
in
i
n
the
t
h
e
gas
g
a
s
and
a
n
d
temperature.
t
e
m
p
e
r
a
t
u
r
e
.
The
T
h
e
overall
o
v
e
r
a
l
l
philosophy
p
h
i
l
o
s
o
p
h
y
used
u
s
e
d
in
i
n
the
t
h
e
selection
s
e
l
e
c
t
i
o
n
of
o
f
materials
m
a
t
e
r
i
a
l
s
and
a
n
d
corrosion
c
o
r
r
o
s
i
o
n
control
c
o
n
t
r
o
l
systems
s
y
s
t
e
m
s
is
i
s
based
b
a
s
e
d
on
o
n
conditions
c
o
n
d
i
t
i
o
n
s
of
o
f
operation
o
p
e
r
a
t
i
o
n
with
w
i
t
h
adequate
a
d
e
q
u
a
t
e
integrity
i
n
t
e
g
r
i
t
y
while
w
h
i
l
e
minimizing
m
i
n
i
m
i
z
i
n
g
capital
c
a
p
i
t
a
l
costs
c
o
s
t
s
and
a
n
d
maintaining
m
a
i
n
t
a
i
n
i
n
g
schedule
s
c
h
e
d
u
l
e
for
f
o
r
fabrication.
f
a
b
r
i
c
a
t
i
o
n
.
Corrosion
C
o
r
r
o
s
i
o
n
shall
s
h
a
l
l
be
b
e
mitigated
m
i
t
i
g
a
t
e
d
by
b
y
sufficient
s
u
f
f
i
c
i
e
n
t
application
a
p
p
l
i
c
a
t
i
o
n
or
o
r
combination
c
o
m
b
i
n
a
t
i
o
n
of
o
f
the
t
h
e
following
f
o
l
l
o
w
i
n
g
methods:
m
e
t
h
o
d
s
:
-
Materials
M
a
t
e
r
i
a
l
s
selection
s
e
l
e
c
t
i
o
n
(corrosion
(
c
o
r
r
o
s
i
o
n
allowance)
a
l
l
o
w
a
n
c
e
)
-
Coatings
C
o
a
t
i
n
g
s
-
Chemical
C
h
e
m
i
c
a
l
treatment
t
r
e
a
t
m
e
n
t
-
Cathodic
C
a
t
h
o
d
i
c
protection
p
r
o
t
e
c
t
i
o
n
-
Corrosion
C
o
r
r
o
s
i
o
n
control/monitoring
c
o
n
t
r
o
l
/
m
o
n
i
t
o
r
i
n
g
The
T
h
e
corrosion
c
o
r
r
o
s
i
o
n
allowances
a
l
l
o
w
a
n
c
e
s
for
f
o
r
pipelines
p
i
p
e
l
i
n
e
s
shall
s
h
a
l
l
be
b
e
specified
s
p
e
c
i
f
i
e
d
with
w
i
t
h
regard
r
e
g
a
r
d
to
t
o
the
t
h
e
corrosion
c
o
r
r
o
s
i
o
n
rates
r
a
t
e
s
calculated
c
a
l
c
u
l
a
t
e
d
after
a
f
t
e
r
taking
t
a
k
i
n
g
into
i
n
t
o
account
a
c
c
o
u
n
t
the
t
h
e
effectiveness
e
f
f
e
c
t
i
v
e
n
e
s
s
of
o
f
inhibition,
i
n
h
i
b
i
t
i
o
n
,
environmental
e
n
v
i
r
o
n
m
e
n
t
a
l
conditioning
c
o
n
d
i
t
i
o
n
i
n
g
and
a
n
d
design
d
e
s
i
g
n
life.
l
i
f
e
.
Generally,
G
e
n
e
r
a
l
l
y
,
process
p
r
o
c
e
s
s
and
a
n
d
corrosive
c
o
r
r
o
s
i
v
e
utilities
u
t
i
l
i
t
i
e
s
equipment
e
q
u
i
p
m
e
n
t
and
a
n
d
piping
p
i
p
i
n
g
shall
s
h
a
l
l
be
b
e
specified
s
p
e
c
i
f
i
e
d
with
w
i
t
h
a
a
minimum
m
i
n
i
m
u
m
3.0
3
.
0
mm
m
m
corrosion
c
o
r
r
o
s
i
o
n
allowance
a
l
l
o
w
a
n
c
e
and
a
n
d
maximum
m
a
x
i
m
u
m
of
o
f
6.0
6
.
0
mm
m
m
corrosion
c
o
r
r
o
s
i
o
n
allowance
a
l
l
o
w
a
n
c
e
while
w
h
i
l
e
pipeline
p
i
p
e
l
i
n
e
can
c
a
n
be
b
e
maximum
m
a
x
i
m
u
m
8
8
or
o
r
10
1
0
mm.
m
m
.
Calculated
C
a
l
c
u
l
a
t
e
d
unhibited
u
n
h
i
b
i
t
e
d
corrosion
c
o
r
r
o
s
i
o
n
rate
r
a
t
e
is
i
s
0.9
0
.
9
mm/yr
m
m
/
y
r
equivalent
e
q
u
i
v
a
l
e
n
t
with
w
i
t
h
8.84
8
.
8
4
mm
m
m
reduction
r
e
d
u
c
t
i
o
n
thickness
t
h
i
c
k
n
e
s
s
during
d
u
r
i
n
g
20
2
0
years
y
e
a
r
s
design
d
e
s
i
g
n
lifetime.
l
i
f
e
t
i
m
e
.
By
B
y
injecting
i
n
j
e
c
t
i
n
g
corrosion
c
o
r
r
o
s
i
o
n
inhibitor
i
n
h
i
b
i
t
o
r
as
a
s
per
p
e
r
document
d
o
c
u
m
e
n
t
Internal
I
n
t
e
r
n
a
l
Corrosion
C
o
r
r
o
s
i
o
n
-
-
Fluids
F
l
u
i
d
s
Classification
C
l
a
s
s
i
f
i
c
a
t
i
o
n
and
a
n
d
Corrosion
C
o
r
r
o
s
i
o
n
Parameters
P
a
r
a
m
e
t
e
r
s
Definition
D
e
f
i
n
i
t
i
o
n
Ref.
R
e
f
.
Doc.
D
o
c
.
02555.VAR.COR.PRG
0
2
5
5
5
.
V
A
R
.
C
O
R
.
P
R
G
which
w
h
i
c
h
may
m
a
y
be
b
e
assumed
a
s
s
u
m
e
d
that
t
h
a
t
inhibition
i
n
h
i
b
i
t
i
o
n
can
c
a
n
decrease
d
e
c
r
e
a
s
e
the
t
h
e
corrosion
c
o
r
r
o
s
i
o
n
rate
r
a
t
e
to
t
o
0.1
0
.
1
mm/year
m
m
/
y
e
a
r
Efficiency
E
f
f
i
c
i
e
n
c
y
inhibitor
i
n
h
i
b
i
t
o
r
will
w
i
l
l
use
u
s
e
formula
f
o
r
m
u
l
a
as
a
s
per
p
e
r
standard.
s
t
a
n
d
a
r
d
.
Corr
C
o
r
r
=
=
(CRinhib
(
C
R
i
n
h
i
b
x
x
lifetime
l
i
f
e
t
i
m
e
x
x
availability)
a
v
a
i
l
a
b
i
l
i
t
y
)
+
+
CRunhib
C
R
u
n
h
i
b
x
x
lifetime
l
i
f
e
t
i
m
e
x
x
un-availability
u
n
-
a
v
a
i
l
a
b
i
l
i
t
y
=
=
(0.1
(
0
.
1
x
x
25
2
5
x
x
0.9)
0
.
9
)
+
+
(CRunhib
(
C
R
u
n
h
i
b
x
x
25
2
5
x
x
0.1)
0
.
1
)
Infield
I
n
f
i
e
l
d
Pipeline,
P
i
p
e
l
i
n
e
,
Formation
F
o
r
m
a
t
i
o
n
Water
W
a
t
e
r
Case
C
a
s
e
Description
D
e
s
c
r
i
p
t
i
o
n
Value
V
a
l
u
e
Unit
U
n
i
t
max.
m
a
x
.
corrosion
c
o
r
r
o
s
i
o
n
rate
r
a
t
e
2.0
2
.
0
mm/y
m
m
/
y
Inhibited
I
n
h
i
b
i
t
e
d
corrosion
c
o
r
r
o
s
i
o
n
rate
r
a
t
e
0.2
0
.
2
mm/y
m
m
/
y
total
t
o
t
a
l
corrosion
c
o
r
r
o
s
i
o
n
allowance
a
l
l
o
w
a
n
c
e
with
w
i
t
h
95%
9
5
%
CI
C
I
4.35
4
.
3
5
mm
m
m
availability
a
v
a
i
l
a
b
i
l
i
t
y
(15
(
1
5
years)
y
e
a
r
s
)
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
The
T
h
e
result
r
e
s
u
l
t
of
o
f
evaluation
e
v
a
l
u
a
t
i
o
n
for
f
o
r
considered
c
o
n
s
i
d
e
r
e
d
only
o
n
l
y
water
w
a
t
e
r
condensed
c
o
n
d
e
n
s
e
d
can
c
a
n
be
b
e
summarized
s
u
m
m
a
r
i
z
e
d
as
a
s
below.
b
e
l
o
w
.
Infield
I
n
f
i
e
l
d
Pipeline,
P
i
p
e
l
i
n
e
,
Condensed
C
o
n
d
e
n
s
e
d
Water
W
a
t
e
r
Case
C
a
s
e
Description
D
e
s
c
r
i
p
t
i
o
n
Value
V
a
l
u
e
Unit
U
n
i
t
max.
m
a
x
.
corrosion
c
o
r
r
o
s
i
o
n
rate
r
a
t
e
2.8
2
.
8
mm/y
m
m
/
y
Inhibited
I
n
h
i
b
i
t
e
d
corrosion
c
o
r
r
o
s
i
o
n
rate
r
a
t
e
0.2
0
.
2
mm/y
m
m
/
y
total
t
o
t
a
l
corrosion
c
o
r
r
o
s
i
o
n
allowance
a
l
l
o
w
a
n
c
e
with
w
i
t
h
95%
9
5
%
CI
C
I
4.95
4
.
9
5
mm
m
m
availability
a
v
a
i
l
a
b
i
l
i
t
y
(15
(
1
5
years)s
y
e
a
r
s
)
s
Based
B
a
s
e
d
on
o
n
the
t
h
e
all
a
l
l
above
a
b
o
v
e
cases,
c
a
s
e
s
,
material
m
a
t
e
r
i
a
l
selection
s
e
l
e
c
t
i
o
n
for
f
o
r
flowline
f
l
o
w
l
i
n
e
is
i
s
calculated
c
a
l
c
u
l
a
t
e
d
as
a
s
CS
C
S
+
+
5
5
mm
m
m
CA
C
A
+
+
>95%
>
9
5
%
of
o
f
corrosion
c
o
r
r
o
s
i
o
n
inhibitor
i
n
h
i
b
i
t
o
r
availability.
a
v
a
i
l
a
b
i
l
i
t
y
.
9.9
9
.
9
Flow
F
l
o
w
Assurance
A
s
s
u
r
a
n
c
e
Issues
I
s
s
u
e
s
For
F
o
r
Flow
F
l
o
w
Assurance
A
s
s
u
r
a
n
c
e
details
d
e
t
a
i
l
s
please
p
l
e
a
s
e
see
s
e
e
ref.
r
e
f
.
9.1.
9
.
1
.
9.10
9
.
1
0
Flowing
F
l
o
w
i
n
g
And
A
n
d
Shut
S
h
u
t
In
I
n
Condition
C
o
n
d
i
t
i
o
n
9.10.1
9
.
1
0
.
1
Flowing
F
l
o
w
i
n
g
Well
W
e
l
l
Head
H
e
a
d
Pressure
P
r
e
s
s
u
r
e
The
T
h
e
flowing
f
l
o
w
i
n
g
well
w
e
l
l
head
h
e
a
d
pressure
p
r
e
s
s
u
r
e
of
o
f
considered
c
o
n
s
i
d
e
r
e
d
for
f
o
r
the
t
h
e
analyses
a
n
a
l
y
s
e
s
are
a
r
e
reported
r
e
p
o
r
t
e
d
below.
b
e
l
o
w
.
Grey
G
r
e
y
cells
c
e
l
l
s
highlight
h
i
g
h
l
i
g
h
t
that
t
h
a
t
the
t
h
e
wells
w
e
l
l
s
or
o
r
cluster
c
l
u
s
t
e
r
is
i
s
closed.
c
l
o
s
e
d
.
Expected
E
x
p
e
c
t
e
d
Mode
M
o
d
e
Date
D
a
t
e
PROJECT
P
R
O
J
E
C
T
PROJECT-4
P
R
O
J
E
C
T
-
4
PROJECT-3
P
R
O
J
E
C
T
-
3
Sep-26
S
e
p
-
2
6
206
2
0
6
196
1
9
6
HP
H
P
mode
m
o
d
e
May-27
M
a
y
-
2
7
152
1
5
2
134
1
3
4
Jun-28
J
u
n
-
2
8
125
1
2
5
110
1
1
0
Dec-29
D
e
c
-
2
9
97
9
7
85
8
5
Jun-30
J
u
n
-
3
0
90
9
0
80
8
0
Jun-31
J
u
n
-
3
1
78
7
8
66
6
6
Jun-32
J
u
n
-
3
2
68
6
8
57
5
7
LP
L
P
mode
m
o
d
e
Jun-33
J
u
n
-
3
3
61
6
1
51
5
1
Jun-34
J
u
n
-
3
4
56
5
6
46
4
6
Jun-35
J
u
n
-
3
5
47
4
7
48
4
8
Dec-36
D
e
c
-
3
6
38
3
8
40
4
0
Jan-37
J
a
n
-
3
7
46
4
6
Table
T
a
b
l
e
12
1
2
–
–
Unconstrained
U
n
c
o
n
s
t
r
a
i
n
e
d
case
c
a
s
e
-
-
FTHP
F
T
H
P
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
9.10.2
9
.
1
0
.
2
Flowing
F
l
o
w
i
n
g
Well
W
e
l
l
Head
H
e
a
d
Temperature
T
e
m
p
e
r
a
t
u
r
e
The
T
h
e
flowing
f
l
o
w
i
n
g
well
w
e
l
l
head
h
e
a
d
temperature
t
e
m
p
e
r
a
t
u
r
e
of
o
f
wells
w
e
l
l
s
considered
c
o
n
s
i
d
e
r
e
d
for
f
o
r
the
t
h
e
analyses
a
n
a
l
y
s
e
s
are
a
r
e
reported
r
e
p
o
r
t
e
d
below.
b
e
l
o
w
.
The
T
h
e
two
t
w
o
tables
t
a
b
l
e
s
report
r
e
p
o
r
t
the
t
h
e
flowing
f
l
o
w
i
n
g
temperature
t
e
m
p
e
r
a
t
u
r
e
upstream
u
p
s
t
r
e
a
m
and
a
n
d
downstream
d
o
w
n
s
t
r
e
a
m
PCVs:
P
C
V
s
:
Flowing
F
l
o
w
i
n
g
Wellhead
W
e
l
l
h
e
a
d
Temperature
T
e
m
p
e
r
a
t
u
r
e
Upstream
U
p
s
t
r
e
a
m
PCV
P
C
V
Date
D
a
t
e
-4
-
4
-3
-
3
Sep-26
S
e
p
-
2
6
59.0
5
9
.
0
60.0
6
0
.
0
May-27
M
a
y
-
2
7
55.0
5
5
.
0
55.0
5
5
.
0
Jun-28
J
u
n
-
2
8
54.0
5
4
.
0
54.0
5
4
.
0
Dec-29
D
e
c
-
2
9
54.0
5
4
.
0
54.0
5
4
.
0
Jun-30
J
u
n
-
3
0
54.0
5
4
.
0
54.0
5
4
.
0
Jun-31
J
u
n
-
3
1
54.0
5
4
.
0
53.0
5
3
.
0
Jun-32
J
u
n
-
3
2
54.0
5
4
.
0
54.0
5
4
.
0
Jun-33
J
u
n
-
3
3
54.0
5
4
.
0
54.0
5
4
.
0
Jun-34
J
u
n
-
3
4
53.0
5
3
.
0
54.0
5
4
.
0
Jun-35
J
u
n
-
3
5
42.0
4
2
.
0
54.0
5
4
.
0
Dec-36
D
e
c
-
3
6
4.0
4
.
0
53.0
5
3
.
0
Jan-37
J
a
n
-
3
7
4.0
4
.
0
47.0
4
7
.
0
Table
T
a
b
l
e
13
1
3
–
–
Unconstrained
U
n
c
o
n
s
t
r
a
i
n
e
d
Case
C
a
s
e
–
–
FTHT
F
T
H
T
u/s
u
/
s
PCV
P
C
V
Flowing
F
l
o
w
i
n
g
Wellhead
W
e
l
l
h
e
a
d
Temperature
T
e
m
p
e
r
a
t
u
r
e
Downstream
D
o
w
n
s
t
r
e
a
m
PCV
P
C
V
Date
D
a
t
e
-4
-
4
-3
-
3
Sep-26
S
e
p
-
2
6
41
4
1
41
4
1
May-27
M
a
y
-
2
7
50
5
0
52
5
2
Jun-28
J
u
n
-
2
8
51
5
1
52
5
2
Dec-29
D
e
c
-
2
9
53
5
3
54
5
4
Jun-30
J
u
n
-
3
0
54
5
4
54
5
4
Jun-31
J
u
n
-
3
1
52
5
2
53
5
3
Jun-32
J
u
n
-
3
2
53
5
3
53
5
3
Jun-33
J
u
n
-
3
3
53
5
3
54
5
4
Jun-34
J
u
n
-
3
4
53
5
3
53
5
3
Jun-35
J
u
n
-
3
5
42
4
2
53
5
3
Dec-36
D
e
c
-
3
6
4
4
53
5
3
Jan-37
J
a
n
-
3
7
4
4
46
4
6
Table
T
a
b
l
e
14
1
4
-
-
Unconstrained
U
n
c
o
n
s
t
r
a
i
n
e
d
Case
C
a
s
e
–
–
FTHT
F
T
H
T
d/s
d
/
s
PCV
P
C
V
9.10.3
9
.
1
0
.
3
Topside
T
o
p
s
i
d
e
Arrival
A
r
r
i
v
a
l
Pressure/Temperature
P
r
e
s
s
u
r
e
/
T
e
m
p
e
r
a
t
u
r
e
As
A
s
per
p
e
r
base
b
a
s
e
case,
c
a
s
e
,
is
i
s
kept
k
e
p
t
in
i
n
production
p
r
o
d
u
c
t
i
o
n
in
i
n
Hybrid
H
y
b
r
i
d
mode
m
o
d
e
(HP
(
H
P
or
o
r
LP)
L
P
)
as
a
s
detailed
d
e
t
a
i
l
e
d
in
i
n
the
t
h
e
previous
p
r
e
v
i
o
u
s
chapters.
c
h
a
p
t
e
r
s
.
The
T
h
e
fluid
f
l
u
i
d
temperature
t
e
m
p
e
r
a
t
u
r
e
at
a
t
FPU
F
P
U
arrival
a
r
r
i
v
a
l
is
i
s
expected
e
x
p
e
c
t
e
d
in
i
n
the
t
h
e
range
r
a
n
g
e
-2-to-10°C,
-
2
-
t
o
-
1
0
°
C
,
the
t
h
e
lorelated
l
o
r
e
l
a
t
e
d
to
t
o
high
h
i
g
h
flowrate.
f
l
o
w
r
a
t
e
.
9.10.3.1
9
.
1
0
.
3
.
1
Operating
O
p
e
r
a
t
i
n
g
Cases
C
a
s
e
s
Base
B
a
s
e
Case
C
a
s
e
-
-
with
w
i
t
h
single
s
i
n
g
l
e
flowline
f
l
o
w
l
i
n
e
connection
c
o
n
n
e
c
t
i
o
n
(Figure
(
F
i
g
u
r
e
6):
6
)
:
the
t
h
e
n.2
n
.
2
new
n
e
w
wells
w
e
l
l
s
are
a
r
e
tied-
t
i
e
d
-
back
b
a
c
k
to
t
o
Jangkrik
J
a
n
g
k
r
i
k
trunkline
t
r
u
n
k
l
i
n
e
1
1
by
b
y
means
m
e
a
n
s
of
o
f
12”
1
2
”
new
n
e
w
subsea
s
u
b
s
e
a
production
p
r
o
d
u
c
t
i
o
n
flowline.
f
l
o
w
l
i
n
e
.
Jangkrik
J
a
n
g
k
r
i
k
Production
P
r
o
d
u
c
t
i
o
n
from
f
r
o
m
Cluster
C
l
u
s
t
e
r
1
1
will
w
i
l
l
be
b
e
sent
s
e
n
t
to
t
o
Jangkrik
J
a
n
g
k
r
i
k
Cluster
C
l
u
s
t
e
r
3.
3
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Figure
F
i
g
u
r
e
6
6
–
–
Field
F
i
e
l
d
Development
D
e
v
e
l
o
p
m
e
n
t
9.10.3.2
9
.
1
0
.
3
.
2
Inlet
I
n
l
e
t
Flowrate
F
l
o
w
r
a
t
e
FPU
F
P
U
JKK
J
K
K
The
T
h
e
following
f
o
l
l
o
w
i
n
g
production
p
r
o
d
u
c
t
i
o
n
cases
c
a
s
e
s
are
a
r
e
selected
s
e
l
e
c
t
e
d
for
f
o
r
design
d
e
s
i
g
n
purposes
p
u
r
p
o
s
e
s
(Table
(
T
a
b
l
e
15)
1
5
)
and
a
n
d
with
w
i
t
h
the
t
h
e
aim
a
i
m
to
t
o
verify
v
e
r
i
f
y
the
t
h
e
existing
e
x
i
s
t
i
n
g
FPU
F
P
U
capacities.
c
a
p
a
c
i
t
i
e
s
.
Field
F
i
e
l
d
TKLs
T
K
L
s
Flowrate
F
l
o
w
r
a
t
e
(MMSCFD)
(
M
M
S
C
F
D
)
Inlet
I
n
l
e
t
Pressure
P
r
e
s
s
u
r
e
(barg)
(
b
a
r
g
)
Slug
S
l
u
g
Catcher
C
a
t
c
h
e
r
223.6
2
2
3
.
6
40
4
0
Jangrkik
J
a
n
g
r
k
i
k
TKL1
T
K
L
1
Jangkrik
J
a
n
g
k
r
i
k
0
0
40
4
0
North
N
o
r
t
h
East
E
a
s
t
Jangkrik
J
a
n
g
k
r
i
k
TKL2
T
K
L
2
11.6
1
1
.
6
25
2
5
TKL3
T
K
L
3
45.3
4
5
.
3
25
2
5
Jangkrik
J
a
n
g
k
r
i
k
NorthEast
N
o
r
t
h
E
a
s
t
TKL4
T
K
L
4
9.71
9
.
7
1
25
2
5
Merakes/Merakes
M
e
r
a
k
e
s
/
M
e
r
a
k
e
s
East
E
a
s
t
TKL5
T
K
L
5
9.71
9
.
7
1
25
2
5
TKL6
T
K
L
6
190
1
9
0
25
2
5
TKL7
T
K
L
7
190
1
9
0
25
2
5
Jangkrik
J
a
n
g
k
r
i
k
Main
M
a
i
n
Merakes
M
e
r
a
k
e
s
East
E
a
s
t
87.5
8
7
.
5
MMSCFD
M
M
S
C
F
D
Merakes
M
e
r
a
k
e
s
292.6
2
9
2
.
6
MMSCFD
M
M
S
C
F
D
-
-
Table
T
a
b
l
e
15:
1
5
:
STRATEGIC
S
T
R
A
T
E
G
I
C
PLAN
P
L
A
N
(MKSE
(
M
K
S
E
SU
S
U
1-Jul-25,
1
-
J
u
l
-
2
5
,
PROJECT
P
R
O
J
E
C
T
SU
S
U
1-Mar-25)
1
-
M
a
r
-
2
5
)
with
w
i
t
h
2.8%DT
2
.
8
%
D
T
JKK/JNE
J
K
K
/
J
N
E
MKS
M
K
S
PROJECT
P
R
O
J
E
C
T
MKSE
M
K
S
E
Flowrate
F
l
o
w
r
a
t
e
[MMSCFD]
[
M
M
S
C
F
D
]
76.37
7
6
.
3
7
292.6
2
9
2
.
6
223.6
2
2
3
.
6
87.5
8
7
.
5
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Slug
S
l
u
g
Catchers
C
a
t
c
h
e
r
s
Capacity:
C
a
p
a
c
i
t
y
:
HP
H
P
Mode
M
o
d
e
LP
L
P
Mode
M
o
d
e
MMSCFD
M
M
S
C
F
D
MMSCFD
M
M
S
C
F
D
JKK
J
K
K
Main
M
a
i
n
SC
S
C
463
4
6
3
342
3
4
2
JKK
J
K
K
NE
N
E
SC
S
C
309
3
0
9
228
2
2
8
Merakes
M
e
r
a
k
e
s
SC
S
C
450
4
5
0
400
4
0
0
For
F
o
r
fields
f
i
e
l
d
s
the
t
h
e
flowrates
f
l
o
w
r
a
t
e
s
for
f
o
r
gas,
g
a
s
,
condensate
c
o
n
d
e
n
s
a
t
e
and
a
n
d
total
t
o
t
a
l
free
f
r
e
e
water
w
a
t
e
r
@Jangkrik
@
J
a
n
g
k
r
i
k
FPU
F
P
U
inlet
i
n
l
e
t
have
h
a
v
e
been
b
e
e
n
extracted
e
x
t
r
a
c
t
e
d
from
f
r
o
m
the
t
h
e
production
p
r
o
d
u
c
t
i
o
n
profiles
p
r
o
f
i
l
e
s
received
r
e
c
e
i
v
e
d
by
b
y
HQ,
H
Q
,
where
w
h
e
r
e
the
t
h
e
gas,
g
a
s
,
condensate
c
o
n
d
e
n
s
a
t
e
and
a
n
d
water
w
a
t
e
r
flowrates
f
l
o
w
r
a
t
e
s
used
u
s
e
d
in
i
n
the
t
h
e
“Sterategic
“
S
t
e
r
a
t
e
g
i
c
Case”
C
a
s
e
”
(i.e.
(
i
.
e
.
the
t
h
e
Dual
D
u
a
l
Mode
M
o
d
e
Case)
C
a
s
e
)
with
w
i
t
h
a
a
maximum
m
a
x
i
m
u
m
export
e
x
p
o
r
t
capacity
c
a
p
a
c
i
t
y
of
o
f
about
a
b
o
u
t
750
7
5
0
MMSCFD
M
M
S
C
F
D
@FPU
@
F
P
U
inlet
i
n
l
e
t
and
a
n
d
with
w
i
t
h
producing
p
r
o
d
u
c
i
n
g
230
2
3
0
MMSCFD
M
M
S
C
F
D
as
a
s
the
t
h
e
maximum
m
a
x
i
m
u
m
plateau
p
l
a
t
e
a
u
in
i
n
HP
H
P
mode
m
o
d
e
and
a
n
d
170MMSCFD
1
7
0
M
M
S
C
F
D
plateau
p
l
a
t
e
a
u
in
i
n
LP
L
P
mode,
m
o
d
e
,
which
w
h
i
c
h
Low
L
o
w
pressure
p
r
e
s
s
u
r
e
with
w
i
t
h
an
a
n
arrival
a
r
r
i
v
a
l
pressure
p
r
e
s
s
u
r
e
of
o
f
25
2
5
barg
b
a
r
g
and
a
n
d
High
H
i
g
h
Pressure
P
r
e
s
s
u
r
e
with
w
i
t
h
an
a
n
arrival
a
r
r
i
v
a
l
pressure
p
r
e
s
s
u
r
e
of
o
f
40
4
0
barg
b
a
r
g
on
o
n
FPU
F
P
U
inlet.
i
n
l
e
t
.
In
I
n
the
t
h
e
following
f
o
l
l
o
w
i
n
g
Table
T
a
b
l
e
16,
1
6
,
shown
s
h
o
w
n
the
t
h
e
gas
g
a
s
flowrate
f
l
o
w
r
a
t
e
in
i
n
the
t
h
e
various
v
a
r
i
o
u
s
trunkline
t
r
u
n
k
l
i
n
e
of
o
f
JKK
J
K
K
FPU
F
P
U
from
f
r
o
m
different
d
i
f
f
e
r
e
n
t
case
c
a
s
e
study
s
t
u
d
y
and
a
n
d
debottlenecking
d
e
b
o
t
t
l
e
n
e
c
k
i
n
g
projects.
p
r
o
j
e
c
t
s
.
HP
H
P
=
=
40
4
0
barg
b
a
r
g
at
a
t
FPU
F
P
U
inlet
i
n
l
e
t
LP
L
P
=
=
25
2
5
barg
b
a
r
g
@
@
FPU
F
P
U
Inlet
I
n
l
e
t
Table
T
a
b
l
e
16:
1
6
:
Design
D
e
s
i
g
n
cases
c
a
s
e
s
from
f
r
o
m
debottlenecking
d
e
b
o
t
t
l
e
n
e
c
k
i
n
g
projects
p
r
o
j
e
c
t
s
-
Case
C
a
s
e
1:
1
:
adjusted
a
d
j
u
s
t
e
d
based
b
a
s
e
d
on
o
n
received
r
e
c
e
i
v
e
d
profiles,
p
r
o
f
i
l
e
s
,
January
J
a
n
u
a
r
y
2024
2
0
2
4
(total
(
t
o
t
a
l
production
p
r
o
d
u
c
t
i
o
n
616
6
1
6
MMSCFD)
M
M
S
C
F
D
)
-
Case
C
a
s
e
2:
2
:
smoothly
s
m
o
o
t
h
l
y
adjusted
a
d
j
u
s
t
e
d
based
b
a
s
e
d
on
o
n
received
r
e
c
e
i
v
e
d
profiles,
p
r
o
f
i
l
e
s
,
July
J
u
l
y
2025
2
0
2
5
(total
(
t
o
t
a
l
production
p
r
o
d
u
c
t
i
o
n
746
7
4
6
MMSCFD)
M
M
S
C
F
D
)
-
Case
C
a
s
e
3:
3
:
as
a
s
per
p
e
r
received
r
e
c
e
i
v
e
d
profiles,
p
r
o
f
i
l
e
s
,
February
F
e
b
r
u
a
r
y
2028.
2
0
2
8
.
Requested
R
e
q
u
e
s
t
e
d
only
o
n
l
y
verification
v
e
r
i
f
i
c
a
t
i
o
n
of
o
f
inlet
i
n
l
e
t
facilities
f
a
c
i
l
i
t
i
e
s
(TKL-1
(
T
K
L
-
1
and
a
n
d
Slug
S
l
u
g
Catcher)
C
a
t
c
h
e
r
)
-
Case
C
a
s
e
4:
4
:
as
a
s
per
p
e
r
received
r
e
c
e
i
v
e
d
profiles,
p
r
o
f
i
l
e
s
,
March
M
a
r
c
h
2023.
2
0
2
3
.
It
I
t
should
s
h
o
u
l
d
be
b
e
covered
c
o
v
e
r
e
d
by
b
y
Case
C
a
s
e
2.
2
.
9.10.3.3
9
.
1
0
.
3
.
3
Target
T
a
r
g
e
t
LP
L
P
Max
M
a
x
Flowrate
F
l
o
w
r
a
t
e
q
q
616
6
1
6
MMSCFD
M
M
S
C
F
D
max
m
a
x
flow
f
l
o
w
in
i
n
LP
L
P
based
b
a
s
e
d
on
o
n
production
p
r
o
d
u
c
t
i
o
n
profile
p
r
o
f
i
l
e
q
q
Maximum
M
a
x
i
m
u
m
production
p
r
o
d
u
c
t
i
o
n
with
w
i
t
h
minor
m
i
n
o
r
modifications
m
o
d
i
f
i
c
a
t
i
o
n
s
-
600
6
0
0
MMSCFD
M
M
S
C
F
D
@
@
LP
L
P
-
Based
B
a
s
e
d
on
o
n
max
m
a
x
seawater
s
e
a
w
a
t
e
r
flowrate
f
l
o
w
r
a
t
e
of
o
f
7500
7
5
0
0
m3/h
m
3
/
h
q
q
720
7
2
0
MMSCFD
M
M
S
C
F
D
Target
T
a
r
g
e
t
FPU
F
P
U
capacity
c
a
p
a
c
i
t
y
in
i
n
LP
L
P
for
f
o
r
DBN
D
B
N
Verification
V
e
r
i
f
i
c
a
t
i
o
n
-
According
A
c
c
o
r
d
i
n
g
to
t
o
previous
p
r
e
v
i
o
u
s
study,
s
t
u
d
y
,
the
t
h
e
same
s
a
m
e
modifications
m
o
d
i
f
i
c
a
t
i
o
n
s
are
a
r
e
required
r
e
q
u
i
r
e
d
above
a
b
o
v
e
600
6
0
0
MMSCFD
M
M
S
C
F
D
in
i
n
LP
L
P
up
u
p
to
t
o
720
7
2
0
MMSCFD
M
M
S
C
F
D
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Seawater
S
e
a
w
a
t
e
r
consumption
c
o
n
s
u
m
p
t
i
o
n
(from
(
f
r
o
m
Saipem
S
a
i
p
e
m
study):
s
t
u
d
y
)
:
~
~
8400
8
4
0
0
m3/h
m
3
/
h
9.11
9
.
1
1
Product
P
r
o
d
u
c
t
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
9.11.1
9
.
1
1
.
1
Produced
P
r
o
d
u
c
e
d
Oil
O
i
l
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
is
i
s
connected
c
o
n
n
e
c
t
e
d
to
t
o
existing
e
x
i
s
t
i
n
g
Jangkrik
J
a
n
g
k
r
i
k
FPU
F
P
U
and
a
n
d
then
t
h
e
n
the
t
h
e
same
s
a
m
e
specification
s
p
e
c
i
f
i
c
a
t
i
o
n
on
o
n
gas
g
a
s
and
a
n
d
condensates
c
o
n
d
e
n
s
a
t
e
s
of
o
f
Jangkrik
J
a
n
g
k
r
i
k
project
p
r
o
j
e
c
t
applies.
a
p
p
l
i
e
s
.
So
S
o
following
f
o
l
l
o
w
i
n
g
specifications
s
p
e
c
i
f
i
c
a
t
i
o
n
s
for
f
o
r
Gas
G
a
s
and
a
n
d
Condensate
C
o
n
d
e
n
s
a
t
e
are
a
r
e
assumed
a
s
s
u
m
e
d
to
t
o
be
b
e
valid
v
a
l
i
d
also
a
l
s
o
for
f
o
r
,
,
based
b
a
s
e
d
on
o
n
Process
P
r
o
c
e
s
s
Basis
B
a
s
i
s
of
o
f
Design
D
e
s
i
g
n
for
f
o
r
Jangkrik
J
a
n
g
k
r
i
k
FPU.
F
P
U
.
Properties
P
r
o
p
e
r
t
i
e
s
Specs
S
p
e
c
s
HC
H
C
Dew
D
e
w
Point
P
o
i
n
t
12°C
1
2
°
C
@
@
any
a
n
y
pressure
p
r
e
s
s
u
r
e
from
f
r
o
m
52
5
2
barg
b
a
r
g
up
u
p
to
t
o
maximum
m
a
x
i
m
u
m
export
e
x
p
o
r
t
pressure;
p
r
e
s
s
u
r
e
;
Water
W
a
t
e
r
Dew
D
e
w
Point
P
o
i
n
t
9°C
9
°
C
@
@
maximum
m
a
x
i
m
u
m
export
e
x
p
o
r
t
pressure
p
r
e
s
s
u
r
e
Associated
A
s
s
o
c
i
a
t
e
d
water
w
a
t
e
r
content
c
o
n
t
e
n
t
9
9
lb/MMSCF
l
b
/
M
M
S
C
F
Table
T
a
b
l
e
17:
1
7
:
Produced
P
r
o
d
u
c
e
d
Specifications
S
p
e
c
i
f
i
c
a
t
i
o
n
s
Properties
P
r
o
p
e
r
t
i
e
s
Specs
S
p
e
c
s
RVP
R
V
P
≤
≤
11
1
1
psia
p
s
i
a
TVP
T
V
P
@
@
40°C
4
0
°
C
≤
≤
13
1
3
psia
p
s
i
a
Water
W
a
t
e
r
Content
C
o
n
t
e
n
t
<
<
0.1%
0
.
1
%
vol.
v
o
l
.
BSW
B
S
W
<
<
10
1
0
PTB
P
T
B
Table
T
a
b
l
e
18:
1
8
:
Sale
S
a
l
e
Condensate
C
o
n
d
e
n
s
a
t
e
Specifications
S
p
e
c
i
f
i
c
a
t
i
o
n
s
9.11.2Produced
9
.
1
1
.
2
P
r
o
d
u
c
e
d
Treated
T
r
e
a
t
e
d
Water
W
a
t
e
r
The
T
h
e
FPU
F
P
U
is
i
s
designed
d
e
s
i
g
n
e
d
to
t
o
handle,
h
a
n
d
l
e
,
treat
t
r
e
a
t
and
a
n
d
dispose
d
i
s
p
o
s
e
the
t
h
e
produced
p
r
o
d
u
c
e
d
water
w
a
t
e
r
and
a
n
d
any
a
n
y
other
o
t
h
e
r
waste
w
a
s
t
e
water
w
a
t
e
r
generated
g
e
n
e
r
a
t
e
d
by
b
y
the
t
h
e
process
p
r
o
c
e
s
s
and
a
n
d
utility
u
t
i
l
i
t
y
units
u
n
i
t
s
aboard
a
b
o
a
r
d
the
t
h
e
FPU.
F
P
U
.
A
A
dedicated
d
e
d
i
c
a
t
e
d
Produced
P
r
o
d
u
c
e
d
Water
W
a
t
e
r
Treatment
T
r
e
a
t
m
e
n
t
unit
u
n
i
t
of
o
f
about
a
b
o
u
t
1150
1
1
5
0
Sbbl/d
S
b
b
l
/
d
is
i
s
available.
a
v
a
i
l
a
b
l
e
.
Treated
T
r
e
a
t
e
d
water
w
a
t
e
r
discharged
d
i
s
c
h
a
r
g
e
d
overboard
o
v
e
r
b
o
a
r
d
shall
s
h
a
l
l
meet
m
e
e
t
the
t
h
e
following
f
o
l
l
o
w
i
n
g
specifications:
s
p
e
c
i
f
i
c
a
t
i
o
n
s
:
-
Maximum
M
a
x
i
m
u
m
HC
H
C
content:
c
o
n
t
e
n
t
:
15
1
5
ppmv
p
p
m
v
(30
(
3
0
days
d
a
y
s
average),
a
v
e
r
a
g
e
)
,
42
4
2
ppmv
p
p
m
v
maximum
m
a
x
i
m
u
m
daily
d
a
i
l
y
peak
p
e
a
k
-
Maximum
M
a
x
i
m
u
m
MEG
M
E
G
content:
c
o
n
t
e
n
t
:
3500
3
5
0
0
ppmv
p
p
m
v
-
Maximum
M
a
x
i
m
u
m
discharge
d
i
s
c
h
a
r
g
e
temperature:
t
e
m
p
e
r
a
t
u
r
e
:
40°C
4
0
°
C
Discharged
D
i
s
c
h
a
r
g
e
d
water
w
a
t
e
r
shall
s
h
a
l
l
be
b
e
continuously
c
o
n
t
i
n
u
o
u
s
l
y
metered
m
e
t
e
r
e
d
and
a
n
d
its
i
t
s
quality
q
u
a
l
i
t
y
continuously
c
o
n
t
i
n
u
o
u
s
l
y
monitored
m
o
n
i
t
o
r
e
d
in
i
n
line
l
i
n
e
with
w
i
t
h
local
l
o
c
a
l
environmental
e
n
v
i
r
o
n
m
e
n
t
a
l
regulations.
r
e
g
u
l
a
t
i
o
n
s
.
On-line
O
n
-
l
i
n
e
analysis
a
n
a
l
y
s
i
s
shall
s
h
a
l
l
be
b
e
based
b
a
s
e
d
on
o
n
Indonesian
I
n
d
o
n
e
s
i
a
n
national
n
a
t
i
o
n
a
l
standard
s
t
a
n
d
a
r
d
SNI
S
N
I
06-6989.10-2004.
0
6
-
6
9
8
9
.
1
0
-
2
0
0
4
.
In
I
n
the
t
h
e
event
e
v
e
n
t
that
t
h
a
t
the
t
h
e
water
w
a
t
e
r
quality
q
u
a
l
i
t
y
requirements
r
e
q
u
i
r
e
m
e
n
t
s
are
a
r
e
not
n
o
t
met,
m
e
t
,
produced
p
r
o
d
u
c
e
d
water
w
a
t
e
r
shall
s
h
a
l
l
be
b
e
automatically
a
u
t
o
m
a
t
i
c
a
l
l
y
routed
r
o
u
t
e
d
to
t
o
the
t
h
e
slop
s
l
o
p
oil
o
i
l
tank.
t
a
n
k
.
A
A
dedicated
d
e
d
i
c
a
t
e
d
hull
h
u
l
l
storage
s
t
o
r
a
g
e
of
o
f
1300
1
3
0
0
m
m
3
3
is
i
s
provided
p
r
o
v
i
d
e
d
for
f
o
r
Treated
T
r
e
a
t
e
d
Water.
W
a
t
e
r
.
9.11.3
9
.
1
1
.
3
H2S
H
2
S
Content
C
o
n
t
e
n
t
The
T
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid
f
l
u
i
d
is
i
s
expected
e
x
p
e
c
t
e
d
to
t
o
be
b
e
H2S
H
2
S
free.
f
r
e
e
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
9.11.4
9
.
1
1
.
4
CO2
C
O
2
Content
C
o
n
t
e
n
t
The
T
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid
f
l
u
i
d
from
f
r
o
m
,
,
as
a
s
evident
e
v
i
d
e
n
t
from
f
r
o
m
the
t
h
e
reservoir
r
e
s
e
r
v
o
i
r
fluid
f
l
u
i
d
compositions
c
o
m
p
o
s
i
t
i
o
n
s
in
i
n
Table
T
a
b
l
e
9,
9
,
shows
s
h
o
w
s
a
a
CO2
C
O
2
content
c
o
n
t
e
n
t
of
o
f
0.92
0
.
9
2
mol
m
o
l
%.
%
.
9.12
9
.
1
2
Field
F
i
e
l
d
Flowrates
F
l
o
w
r
a
t
e
s
for
f
o
r
Design
D
e
s
i
g
n
Purpose
P
u
r
p
o
s
e
The
T
h
e
following
f
o
l
l
o
w
i
n
g
production
p
r
o
d
u
c
t
i
o
n
cases
c
a
s
e
s
are
a
r
e
selected
s
e
l
e
c
t
e
d
for
f
o
r
design
d
e
s
i
g
n
purposes
p
u
r
p
o
s
e
s
(Table
(
T
a
b
l
e
19)
1
9
)
and
a
n
d
with
w
i
t
h
the
t
h
e
aim
a
i
m
to
t
o
verify
v
e
r
i
f
y
the
t
h
e
existing
e
x
i
s
t
i
n
g
FPU
F
P
U
capacities
c
a
p
a
c
i
t
i
e
s
Fluid
F
l
u
i
d
HP
H
P
Inlet
I
n
l
e
t
Gas
G
a
s
[MMSCFD]
[
M
M
S
C
F
D
]
223.6
2
2
3
.
6
Inlet
I
n
l
e
t
Condensate
C
o
n
d
e
n
s
a
t
e
[Sbbl/d]
[
S
b
b
l
/
d
]
1303.5
1
3
0
3
.
5
Inlet
I
n
l
e
t
Water
W
a
t
e
r
[Sbbl/d]
[
S
b
b
l
/
d
]
0.68
0
.
6
8
Table
T
a
b
l
e
19
1
9
-
-
Development
D
e
v
e
l
o
p
m
e
n
t
-
-
Design
D
e
s
i
g
n
cases
c
a
s
e
s
For
F
o
r
field
f
i
e
l
d
the
t
h
e
flowrates
f
l
o
w
r
a
t
e
s
for
f
o
r
gas,
g
a
s
,
condensate
c
o
n
d
e
n
s
a
t
e
and
a
n
d
total
t
o
t
a
l
free
f
r
e
e
water
w
a
t
e
r
@Jangkrik
@
J
a
n
g
k
r
i
k
FPU
F
P
U
inlet
i
n
l
e
t
have
h
a
v
e
been
b
e
e
n
extracted
e
x
t
r
a
c
t
e
d
from
f
r
o
m
the
t
h
e
production
p
r
o
d
u
c
t
i
o
n
profiles
p
r
o
f
i
l
e
s
received
r
e
c
e
i
v
e
d
by
b
y
Reservoir
R
e
s
e
r
v
o
i
r
HQ.
H
Q
.
The
T
h
e
saturation
s
a
t
u
r
a
t
i
o
n
water
w
a
t
e
r
and
a
n
d
MEG
M
E
G
associated
a
s
s
o
c
i
a
t
e
d
to
t
o
Jangkrik
J
a
n
g
k
r
i
k
has
h
a
s
been
b
e
e
n
prorated
p
r
o
r
a
t
e
d
according
a
c
c
o
r
d
i
n
g
to
t
o
the
t
h
e
new
n
e
w
gas
g
a
s
flowrates
f
l
o
w
r
a
t
e
s
taking
t
a
k
i
n
g
into
i
n
t
o
by
b
y
assuming
a
s
s
u
m
i
n
g
the
t
h
e
same
s
a
m
e
corresponding
c
o
r
r
e
s
p
o
n
d
i
n
g
pro-rating
p
r
o
-
r
a
t
i
n
g
values
v
a
l
u
e
s
used
u
s
e
d
for
f
o
r
Jangkrik
J
a
n
g
k
r
i
k
Main.
M
a
i
n
.
10
1
0
FACILITIES
F
A
C
I
L
I
T
I
E
S
10.1
1
0
.
1
Subsea,
S
u
b
s
e
a
,
Umbilical
U
m
b
i
l
i
c
a
l
and
a
n
d
Flowlines
F
l
o
w
l
i
n
e
s
In
I
n
the
t
h
e
following,
f
o
l
l
o
w
i
n
g
,
a
a
description
d
e
s
c
r
i
p
t
i
o
n
of
o
f
the
t
h
e
subsea
s
u
b
s
e
a
system
s
y
s
t
e
m
(incl.
(
i
n
c
l
.
umbilical
u
m
b
i
l
i
c
a
l
and
a
n
d
subsea
s
u
b
s
e
a
structures)
s
t
r
u
c
t
u
r
e
s
)
and
a
n
d
flexible
f
l
e
x
i
b
l
e
flowline
f
l
o
w
l
i
n
e
system
s
y
s
t
e
m
foreseen
f
o
r
e
s
e
e
n
for
f
o
r
the
t
h
e
field
f
i
e
l
d
is
i
s
provided.
p
r
o
v
i
d
e
d
.
10.1.1
1
0
.
1
.
1
FPU
F
P
U
For
F
o
r
a
a
FPU
F
P
U
Process
P
r
o
c
e
s
s
Description,
D
e
s
c
r
i
p
t
i
o
n
,
refer
r
e
f
e
r
to
t
o
[22].
[
2
2
]
.
10.1.2
1
0
.
1
.
2
Design
D
e
s
i
g
n
Life
L
i
f
e
The
T
h
e
design
d
e
s
i
g
n
life
l
i
f
e
of
o
f
the
t
h
e
subsea
s
u
b
s
e
a
production
p
r
o
d
u
c
t
i
o
n
and
a
n
d
control
c
o
n
t
r
o
l
system
s
y
s
t
e
m
shall
s
h
a
l
l
be
b
e
20
2
0
years.
y
e
a
r
s
.
10.1.3
1
0
.
1
.
3
Maximum
M
a
x
i
m
u
m
Water
W
a
t
e
r
Depth
D
e
p
t
h
The
T
h
e
whole
w
h
o
l
e
subsea
s
u
b
s
e
a
system
s
y
s
t
e
m
shall
s
h
a
l
l
be
b
e
designed
d
e
s
i
g
n
e
d
for
f
o
r
1.200m
1
.
2
0
0
m
of
o
f
water
w
a
t
e
r
depth.
d
e
p
t
h
.
10.1.4
1
0
.
1
.
4
Main
M
a
i
n
Subsea
S
u
b
s
e
a
Equipment
E
q
u
i
p
m
e
n
t
A
A
preliminary
p
r
e
l
i
m
i
n
a
r
y
subsea
s
u
b
s
e
a
equipment
e
q
u
i
p
m
e
n
t
list
l
i
s
t
and
a
n
d
related
r
e
l
a
t
e
d
design
d
e
s
i
g
n
data
d
a
t
a
is
i
s
provided
p
r
o
v
i
d
e
d
in
i
n
the
t
h
e
below
b
e
l
o
w
tables.
t
a
b
l
e
s
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Item
I
t
e
m
Quantity
Q
u
a
n
t
i
t
y
Design
D
e
s
i
g
n
Pressure
P
r
e
s
s
u
r
e
Design
D
e
s
i
g
n
Temperature
T
e
m
p
e
r
a
t
u
r
e
Production
P
r
o
d
u
c
t
i
o
n
Xmas
X
m
a
s
Tree
T
r
e
e
2
2
10.000
1
0
.
0
0
0
psi
p
s
i
Upstream
U
p
s
t
r
e
a
m
the
t
h
e
choke:
c
h
o
k
e
:
-18/+121
-
1
8
/
+
1
2
1
°C
°
C
(1)
(
1
)
Downstream
D
o
w
n
s
t
r
e
a
m
the
t
h
e
choke
c
h
o
k
e
(included):
(
i
n
c
l
u
d
e
d
)
:
-48/+121
-
4
8
/
+
1
2
1
°C
°
C
HIPPS
H
I
P
P
S
System
S
y
s
t
e
m
1
1
(i)
(
i
)
270
2
7
0
Bar
B
a
r
Header
H
e
a
d
e
r
from
f
r
o
m
HBV1
H
B
V
1
(valve
(
v
a
l
v
e
not
n
o
t
included)
i
n
c
l
u
d
e
d
)
to
t
o
inboard
i
n
b
o
a
r
d
connector,
c
o
n
n
e
c
t
o
r
,
Header
H
e
a
d
e
r
from
f
r
o
m
TIV1
T
I
V
1
(valve
(
v
a
l
v
e
not
n
o
t
included)
i
n
c
l
u
d
e
d
)
to
t
o
inboard
i
n
b
o
a
r
d
connector
c
o
n
n
e
c
t
o
r
&
&
adjoining
a
d
j
o
i
n
i
n
g
Hot
H
o
t
Stab
S
t
a
b
lines;
l
i
n
e
s
;
(ii)
(
i
i
)
421
4
2
1
Bar
B
a
r
remaining
r
e
m
a
i
n
i
n
g
parts
p
a
r
t
s
of
o
f
Header,
H
e
a
d
e
r
,
header
h
e
a
d
e
r
valves
v
a
l
v
e
s
and
a
n
d
chemical
c
h
e
m
i
c
a
l
injection
i
n
j
e
c
t
i
o
n
lines
l
i
n
e
s
-20/+70°C
-
2
0
/
+
7
0
°
C
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
TEE
T
E
E
Structure
S
t
r
u
c
t
u
r
e
1
1
&
&
test
t
e
s
t
port
p
o
r
t
lines.
l
i
n
e
s
.
270
2
7
0
bar
b
a
r
for
f
o
r
header,
h
e
a
d
e
r
,
650
6
5
0
for
f
o
r
branch
b
r
a
n
c
h
up
u
p
to
t
o
branch
b
r
a
n
c
h
valve
v
a
l
v
e
(valve
(
v
a
l
v
e
included)
i
n
c
l
u
d
e
d
)
-20/+70°C
-
2
0
/
+
7
0
°
C
Subsea
S
u
b
s
e
a
Structure
S
t
r
u
c
t
u
r
e
4
4
Hub
H
u
b
1
1
520
5
2
0
bar
b
a
r
for
f
o
r
all
a
l
l
parts
p
a
r
t
s
of
o
f
the
t
h
e
structure
s
t
r
u
c
t
u
r
e
exception
e
x
c
e
p
t
i
o
n
made
m
a
d
e
for
f
o
r
the
t
h
e
header
h
e
a
d
e
r
connectors
c
o
n
n
e
c
t
o
r
s
(270
(
2
7
0
bar)
b
a
r
)
-29/+70°C
-
2
9
/
+
7
0
°
C
UTA
U
T
A
1-off
1
-
o
f
f
–
–
Project
P
r
o
j
e
c
t
UMB1
U
M
B
1
UTA
U
T
A
A
A
1-off
1
-
o
f
f
–
–
Project
P
r
o
j
e
c
t
UMB1
U
M
B
1
UTA
U
T
A
B
B
1-off
1
-
o
f
f
–
–
Project
P
r
o
j
e
c
t
UMB2
U
M
B
2
UTA
U
T
A
A
A
1-off
1
-
o
f
f
–
–
Project
P
r
o
j
e
c
t
UMB2
U
M
B
2
UTA
U
T
A
B
B
FLET
F
L
E
T
1
1
TBD
T
B
D
TBD
T
B
D
Table
T
a
b
l
e
20:
2
0
:
Preliminary
P
r
e
l
i
m
i
n
a
r
y
list
l
i
s
t
of
o
f
main
m
a
i
n
subsea
s
u
b
s
e
a
equipment
e
q
u
i
p
m
e
n
t
-
As
A
s
per
p
e
r
Merakes
M
e
r
a
k
e
s
XTR
X
T
R
-
MEG
M
E
G
pump
p
u
m
p
design
d
e
s
i
g
n
pressure
p
r
e
s
s
u
r
e
=
=
340
3
4
0
barg
b
a
r
g
(PSV
(
P
S
V
set
s
e
t
point).
p
o
i
n
t
)
.
Including
I
n
c
l
u
d
i
n
g
Pressure
P
r
e
s
s
u
r
e
head
h
e
a
d
at
a
t
1200m
1
2
0
0
m
is
i
s
therefore
t
h
e
r
e
f
o
r
e
equal
e
q
u
a
l
to
t
o
340
3
4
0
barg
b
a
r
g
+
+
130bar
1
3
0
b
a
r
=
=
470
4
7
0
bar.
b
a
r
.
See
S
e
e
Ref.
R
e
f
.
[32]
[
3
2
]
for
f
o
r
Design
D
e
s
i
g
n
pressure
p
r
e
s
s
u
r
e
definition
d
e
f
i
n
i
t
i
o
n
due
d
u
e
to
t
o
MEG
M
E
G
packing
p
a
c
k
i
n
g
condition.
c
o
n
d
i
t
i
o
n
.
-
3&2&4WHSIP*1.1=242.2*1.1=270bar
3
&
2
&
4
W
H
S
I
P
*
1
.
1
=
2
4
2
.
2
*
1
.
1
=
2
7
0
b
a
r
-
DT=Max
D
T
=
M
a
x
operating
o
p
e
r
a
t
i
n
g
(55Deg)
(
5
5
D
e
g
)
plus
p
l
u
s
15Deg
1
5
D
e
g
of
o
f
contingency
c
o
n
t
i
n
g
e
n
c
y
-
A
A
new
n
e
w
FLET
F
L
E
T
is
i
s
foreseen
f
o
r
e
s
e
e
n
for
f
o
r
connecting
c
o
n
n
e
c
t
i
n
g
the
t
h
e
Jangkrik
J
a
n
g
k
r
i
k
Cluster
C
l
u
s
t
e
r
1
1
to
t
o
Jangkrik
J
a
n
g
k
r
i
k
Cluster
C
l
u
s
t
e
r
3
3
already
a
l
r
e
a
d
y
existing
e
x
i
s
t
i
n
g
FLET
F
L
E
T
1,
1
,
through
t
h
r
o
u
g
h
a
a
new
n
e
w
Interconnecting
I
n
t
e
r
c
o
n
n
e
c
t
i
n
g
Line
L
i
n
e
HIPPS
H
I
P
P
S
valve
v
a
l
v
e
set
s
e
t
point
p
o
i
n
t
max
m
a
x
flowing
f
l
o
w
i
n
g
plus
p
l
u
s
contingency
c
o
n
t
i
n
g
e
n
c
y
=
=
110bar
1
1
0
b
a
r
Note:
N
o
t
e
:
As
A
s
contingency
c
o
n
t
i
n
g
e
n
c
y
approach,
a
p
p
r
o
a
c
h
,
the
t
h
e
DP
D
P
of
o
f
7500psi
7
5
0
0
p
s
i
is
i
s
considering
c
o
n
s
i
d
e
r
i
n
g
potential
p
o
t
e
n
t
i
a
l
closure
c
l
o
s
u
r
e
of
o
f
Subsea
S
u
b
s
e
a
Structure
S
t
r
u
c
t
u
r
e
valve
v
a
l
v
e
by
b
y
mistake
m
i
s
t
a
k
e
during
d
u
r
i
n
g
installation
i
n
s
t
a
l
l
a
t
i
o
n
of
o
f
operation
o
p
e
r
a
t
i
o
n
phase.
p
h
a
s
e
.
As
A
s
consequence,
c
o
n
s
e
q
u
e
n
c
e
,
the
t
h
e
DP
D
P
of
o
f
Subsea
S
u
b
s
e
a
Structure
S
t
r
u
c
t
u
r
e
and
a
n
d
welljumper
w
e
l
l
j
u
m
p
e
r
is
i
s
driven
d
r
i
v
e
n
by
b
y
MEG
M
E
G
packing
p
a
c
k
i
n
g
(see
(
s
e
e
note
n
o
t
e
(2)).
(
2
)
)
.
10.1.5
1
0
.
1
.
5
Umbilicals
U
m
b
i
l
i
c
a
l
s
In
I
n
order
o
r
d
e
r
to
t
o
control
c
o
n
t
r
o
l
the
t
h
e
Subsea
S
u
b
s
e
a
Production
P
r
o
d
u
c
t
i
o
n
System
S
y
s
t
e
m
a
a
dedicated
d
e
d
i
c
a
t
e
d
electro-hydraulic
e
l
e
c
t
r
o
-
h
y
d
r
a
u
l
i
c
umbilical
u
m
b
i
l
i
c
a
l
system
s
y
s
t
e
m
will
w
i
l
l
be
b
e
installed.
i
n
s
t
a
l
l
e
d
.
The
T
h
e
umbilical
u
m
b
i
l
i
c
a
l
will
w
i
l
l
supply
s
u
p
p
l
y
to
t
o
Subsea
S
u
b
s
e
a
Production
P
r
o
d
u
c
t
i
o
n
System
S
y
s
t
e
m
equipment
e
q
u
i
p
m
e
n
t
the
t
h
e
hydraulic
h
y
d
r
a
u
l
i
c
power,
p
o
w
e
r
,
chemicals,
c
h
e
m
i
c
a
l
s
,
electrical
e
l
e
c
t
r
i
c
a
l
power
p
o
w
e
r
and
a
n
d
control
c
o
n
t
r
o
l
signals,
s
i
g
n
a
l
s
,
see
s
e
e
ref.
r
e
f
.
[12].
[
1
2
]
.
The
T
h
e
following
f
o
l
l
o
w
i
n
g
scenario
s
c
e
n
a
r
i
o
will
w
i
l
l
be
b
e
considered
c
o
n
s
i
d
e
r
e
d
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Umbilical
U
m
b
i
l
i
c
a
l
from
f
r
o
m
JKK
J
K
K
Cluster
C
l
u
s
t
e
r
1:
1
:
This
T
h
i
s
scenario
s
c
e
n
a
r
i
o
considers
c
o
n
s
i
d
e
r
s
using
u
s
i
n
g
the
t
h
e
existing
e
x
i
s
t
i
n
g
JKK
J
K
K
Main
M
a
i
n
UMB
U
M
B
1
1
to
t
o
control
c
o
n
t
r
o
l
Field.
F
i
e
l
d
.
An
A
n
assessment
a
s
s
e
s
s
m
e
n
t
was
w
a
s
performed
p
e
r
f
o
r
m
e
d
by
b
y
subsea
s
u
b
s
e
a
control
c
o
n
t
r
o
l
vendor
v
e
n
d
o
r
(refer
(
r
e
f
e
r
to
t
o
feasibility
f
e
a
s
i
b
i
l
i
t
y
study
s
t
u
d
y
for
f
o
r
details).
d
e
t
a
i
l
s
)
.
Errore.
E
r
r
o
r
e
.
L'origine
L
'
o
r
i
g
i
n
e
riferimento
r
i
f
e
r
i
m
e
n
t
o
non
n
o
n
è
è
stata
s
t
a
t
a
trovata.For
t
r
o
v
a
t
a
.
F
o
r
such
s
u
c
h
scenario
s
c
e
n
a
r
i
o
the
t
h
e
network
n
e
t
w
o
r
k
of
o
f
UMBILICAL
U
M
B
I
L
I
C
A
L
consist
c
o
n
s
i
s
t
in:
i
n
:
-
UMB1:
U
M
B
1
:
flying
f
l
y
i
n
g
leads
l
e
a
d
s
connect
c
o
n
n
e
c
t
UMB1
U
M
B
1
UTA
U
T
A
A
A
to
t
o
JKK
J
K
K
Cluster
C
l
u
s
t
e
r
1
1
SDU
S
D
U
and
a
n
d
to
t
o
HIPPS,
H
I
P
P
S
,
all
a
l
l
located
l
o
c
a
t
e
d
near
n
e
a
r
JKK
J
K
K
Cluster
C
l
u
s
t
e
r
1.
1
.
UMB1
U
M
B
1
UTA
U
T
A
B
B
connects
c
o
n
n
e
c
t
s
to
t
o
3b
3
b
and
a
n
d
to
t
o
Project
P
r
o
j
e
c
t
UMB2
U
M
B
2
UTA
U
T
A
A
A
via
v
i
a
flying
f
l
y
i
n
g
leads.
l
e
a
d
s
.
-
UMB2:
U
M
B
2
:
UMB2
U
M
B
2
is
i
s
connected
c
o
n
n
e
c
t
e
d
in
i
n
daisy-chain
d
a
i
s
y
-
c
h
a
i
n
to
t
o
UMB1
U
M
B
1
via
v
i
a
flying
f
l
y
i
n
g
leads.
l
e
a
d
s
.
UMB2
U
M
B
2
UTA
U
T
A
B
B
connects
c
o
n
n
e
c
t
s
to
t
o
4
4
Xtree
X
t
r
e
e
via
v
i
a
flying
f
l
y
i
n
g
leads.
l
e
a
d
s
.
Block
B
l
o
c
k
Diagram
D
i
a
g
r
a
m
for
f
o
r
this
t
h
i
s
scenario
s
c
e
n
a
r
i
o
is
i
s
in
i
n
Ref
R
e
f
[2].
[
2
]
.
For
F
o
r
further
f
u
r
t
h
e
r
details
d
e
t
a
i
l
s
of
o
f
the
t
h
e
umbilical
u
m
b
i
l
i
c
a
l
system
s
y
s
t
e
m
refer
r
e
f
e
r
to
t
o
Ref
R
e
f
[31].
[
3
1
]
.
In
I
n
order
o
r
d
e
r
to
t
o
benefit
b
e
n
e
f
i
t
from
f
r
o
m
existing
e
x
i
s
t
i
n
g
design
d
e
s
i
g
n
and
a
n
d
equipment,
e
q
u
i
p
m
e
n
t
,
the
t
h
e
spare
s
p
a
r
e
umbilical
u
m
b
i
l
i
c
a
l
of
o
f
Merakes
M
e
r
a
k
e
s
infield
i
n
f
i
e
l
d
UM1C
U
M
1
C
will
w
i
l
l
be
b
e
used
u
s
e
d
for
f
o
r
UMB2.The
U
M
B
2
.
T
h
e
umbilical
u
m
b
i
l
i
c
a
l
UMB1
U
M
B
1
shall
s
h
a
l
l
be
b
e
designed
d
e
s
i
g
n
e
d
to
t
o
support
s
u
p
p
o
r
t
the
t
h
e
control
c
o
n
t
r
o
l
of
o
f
the
t
h
e
HIPPS
H
I
P
P
S
module,
m
o
d
u
l
e
,
3b
3
b
and
a
n
d
4.
4
.
The
T
h
e
base
b
a
s
e
case
c
a
s
e
is
i
s
to
t
o
avoid
a
v
o
i
d
additional
a
d
d
i
t
i
o
n
a
l
design
d
e
s
i
g
n
variant,
v
a
r
i
a
n
t
,
therefore
t
h
e
r
e
f
o
r
e
to
t
o
use
u
s
e
same
s
a
m
e
design
d
e
s
i
g
n
as
a
s
UMB2
U
M
B
2
.
.
The
T
h
e
aim
a
i
m
is
i
s
to
t
o
to
t
o
minimize
m
i
n
i
m
i
z
e
customized
c
u
s
t
o
m
i
z
e
d
design
d
e
s
i
g
n
and
a
n
d
engineering
e
n
g
i
n
e
e
r
i
n
g
activities
a
c
t
i
v
i
t
i
e
s
for
f
o
r
project;
p
r
o
j
e
c
t
;
however,
h
o
w
e
v
e
r
,
further
f
u
r
t
h
e
r
optimisation
o
p
t
i
m
i
s
a
t
i
o
n
may
m
a
y
be
b
e
evaluated
e
v
a
l
u
a
t
e
d
for
f
o
r
the
t
h
e
UMB1
U
M
B
1
design,e.g.
d
e
s
i
g
n
,
e
.
g
.
1-off
1
-
o
f
f
1.5”
1
.
5
”
MEG.
M
E
G
.
10.1.6
1
0
.
1
.
6
Control
C
o
n
t
r
o
l
System
S
y
s
t
e
m
Description
D
e
s
c
r
i
p
t
i
o
n
Each
E
a
c
h
Xtree
X
t
r
e
e
and
a
n
d
HIPPS
H
I
P
P
S
will
w
i
l
l
be
b
e
controlled
c
o
n
t
r
o
l
l
e
d
by
b
y
its
i
t
s
dedicated
d
e
d
i
c
a
t
e
d
SCM.
S
C
M
.
Flying
F
l
y
i
n
g
leads
l
e
a
d
s
will
w
i
l
l
distribute
d
i
s
t
r
i
b
u
t
e
control
c
o
n
t
r
o
l
to
t
o
the
t
h
e
SCMs
S
C
M
s
frm
f
r
m
the
t
h
e
UTAs
U
T
A
s
to
t
o
the
t
h
e
host
h
o
s
t
structures.
s
t
r
u
c
t
u
r
e
s
.
The
T
h
e
subsea
s
u
b
s
e
a
control
c
o
n
t
r
o
l
system
s
y
s
t
e
m
shall
s
h
a
l
l
be
b
e
compatible
c
o
m
p
a
t
i
b
l
e
with
w
i
t
h
the
t
h
e
existing
e
x
i
s
t
i
n
g
subsea
s
u
b
s
e
a
control
c
o
n
t
r
o
l
system
s
y
s
t
e
m
and
a
n
d
be
b
e
designed
d
e
s
i
g
n
e
d
in
i
n
accordance
a
c
c
o
r
d
a
n
c
e
with
w
i
t
h
company
c
o
m
p
a
n
y
standard
s
t
a
n
d
a
r
d
18010.ENG.STA.STD;
1
8
0
1
0
.
E
N
G
.
S
T
A
.
S
T
D
;
HIPPS
H
I
P
P
S
shall
s
h
a
l
l
be
b
e
designed
d
e
s
i
g
n
e
d
based
b
a
s
e
d
on
o
n
requirements
r
e
q
u
i
r
e
m
e
n
t
s
stated
s
t
a
t
e
d
inside
i
n
s
i
d
e
28746.ENG.STA.STD.
2
8
7
4
6
.
E
N
G
.
S
T
A
.
S
T
D
.
Communication
C
o
m
m
u
n
i
c
a
t
i
o
n
type
t
y
p
e
will
w
i
l
l
be
b
e
“Communications
“
C
o
m
m
u
n
i
c
a
t
i
o
n
s
On
O
n
Power”
P
o
w
e
r
”
(COPS)
(
C
O
P
S
)
and
a
n
d
the
t
h
e
hydraulic
h
y
d
r
a
u
l
i
c
system
s
y
s
t
e
m
will
w
i
l
l
be
b
e
closed
c
l
o
s
e
d
loop
l
o
o
p
with
w
i
t
h
a
a
return
r
e
t
u
r
n
line
l
i
n
e
from
f
r
o
m
subsea
s
u
b
s
e
a
to
t
o
surface.
s
u
r
f
a
c
e
.
The
T
h
e
susbsea
s
u
s
b
s
e
a
system
s
y
s
t
e
m
will
w
i
l
l
be
b
e
controlled
c
o
n
t
r
o
l
l
e
d
topside
t
o
p
s
i
d
e
by
b
y
the
t
h
e
existing
e
x
i
s
t
i
n
g
Jangkrik
J
a
n
g
k
r
i
k
topside
t
o
p
s
i
d
e
control
c
o
n
t
r
o
l
system.
s
y
s
t
e
m
.
Modifications
M
o
d
i
f
i
c
a
t
i
o
n
s
to
t
o
the
t
h
e
existing
e
x
i
s
t
i
n
g
topside
t
o
p
s
i
d
e
facilities
f
a
c
i
l
i
t
i
e
s
will
w
i
l
l
be
b
e
required
r
e
q
u
i
r
e
d
and
a
n
d
include
i
n
c
l
u
d
e
software
s
o
f
t
w
a
r
e
and
a
n
d
hardware
h
a
r
d
w
a
r
e
updates.
u
p
d
a
t
e
s
.
Hardware
H
a
r
d
w
a
r
e
updates
u
p
d
a
t
e
s
may
m
a
y
be
b
e
carried
c
a
r
r
i
e
d
out
o
u
t
one
o
n
e
channel
c
h
a
n
n
e
l
at
a
t
a
a
time
t
i
m
e
and
a
n
d
therefore
t
h
e
r
e
f
o
r
e
could
c
o
u
l
d
potentially
p
o
t
e
n
t
i
a
l
l
y
be
b
e
executed
e
x
e
c
u
t
e
d
without
w
i
t
h
o
u
t
need
n
e
e
d
to
t
o
shutdown
s
h
u
t
d
o
w
n
JKK
J
K
K
cluster
c
l
u
s
t
e
r
1.
1
.
However,
H
o
w
e
v
e
r
,
software
s
o
f
t
w
a
r
e
updates
u
p
d
a
t
e
s
on
o
n
the
t
h
e
topside
t
o
p
s
i
d
e
system
s
y
s
t
e
m
may
m
a
y
require
r
e
q
u
i
r
e
production
p
r
o
d
u
c
t
i
o
n
shutdown.
s
h
u
t
d
o
w
n
.
For
F
o
r
more
m
o
r
e
details
d
e
t
a
i
l
s
see
s
e
e
[30][31].
[
3
0
]
[
3
1
]
.
10.1.7
1
0
.
1
.
7
Flowlines
F
l
o
w
l
i
n
e
s
System
S
y
s
t
e
m
Flexible
F
l
e
x
i
b
l
e
pipeline
p
i
p
e
l
i
n
e
shall
s
h
a
l
l
be
b
e
considered
c
o
n
s
i
d
e
r
e
d
for
f
o
r
the
t
h
e
development
d
e
v
e
l
o
p
m
e
n
t
of
o
f
the
t
h
e
development
d
e
v
e
l
o
p
m
e
n
t
project.
p
r
o
j
e
c
t
.
The
T
h
e
below
b
e
l
o
w
table
t
a
b
l
e
includes
i
n
c
l
u
d
e
s
all
a
l
l
the
t
h
e
design
d
e
s
i
g
n
input
i
n
p
u
t
to
t
o
be
b
e
consiered
c
o
n
s
i
e
r
e
d
for
f
o
r
the
t
h
e
flexible
f
l
e
x
i
b
l
e
pipeline
p
i
p
e
l
i
n
e
design
d
e
s
i
g
n
and
a
n
d
routing
r
o
u
t
i
n
g
analysis.
a
n
a
l
y
s
i
s
.
Preliminary
P
r
e
l
i
m
i
n
a
r
y
indications
i
n
d
i
c
a
t
i
o
n
s
on
o
n
flexible
f
l
e
x
i
b
l
e
jumpers
j
u
m
p
e
r
s
are
a
r
e
also
a
l
s
o
included.
i
n
c
l
u
d
e
d
.
Standard
S
t
a
n
d
a
r
d
23020.ENG.SSE.STD
2
3
0
2
0
.
E
N
G
.
S
S
E
.
S
T
D
International
I
n
t
e
r
n
a
t
i
o
n
a
l
Code
C
o
d
e
API
A
P
I
17B
1
7
B
API
A
P
I
17J
1
7
J
Inside
I
n
s
i
d
e
Diameter
D
i
a
m
e
t
e
r
for
f
o
r
flowline
f
l
o
w
l
i
n
e
1
1
and
a
n
d
2
2
12”
1
2
”
–
–
304.8
3
0
4
.
8
mm
m
m
Inside
I
n
s
i
d
e
Diameter
D
i
a
m
e
t
e
r
for
f
o
r
flowline
f
l
o
w
l
i
n
e
3
3
11.5”
1
1
.
5
”
–
–
292
2
9
2
mm
m
m
(*)
(
*
)
Inside
I
n
s
i
d
e
Diameter
D
i
a
m
e
t
e
r
for
f
o
r
Flexible
F
l
e
x
i
b
l
e
Jumper
J
u
m
p
e
r
(**)
(
*
*
)
12”
1
2
”
–
–
304.8
3
0
4
.
8
mm
m
m
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Inside
I
n
s
i
d
e
Diameter
D
i
a
m
e
t
e
r
for
f
o
r
Well
W
e
l
l
Jumpers
J
u
m
p
e
r
s
8”
8
”
ID
I
D
Inside
I
n
s
i
d
e
Diameter
D
i
a
m
e
t
e
r
for
f
o
r
Interconnecting
I
n
t
e
r
c
o
n
n
e
c
t
i
n
g
Flowline
F
l
o
w
l
i
n
e
8”
8
”
ID
I
D
Design
D
e
s
i
g
n
Temperature
T
e
m
p
e
r
a
t
u
r
e
70°C
7
0
°
C
Design
D
e
s
i
g
n
Pressure
P
r
e
s
s
u
r
e
for
f
o
r
flexible
f
l
e
x
i
b
l
e
flowline
f
l
o
w
l
i
n
e
1,
1
,
2
2
270
2
7
0
bar
b
a
r
Interconnecting
I
n
t
e
r
c
o
n
n
e
c
t
i
n
g
flowline
f
l
o
w
l
i
n
e
205
2
0
5
bar
b
a
r
Design
D
e
s
i
g
n
Pressure
P
r
e
s
s
u
r
e
for
f
o
r
Flexible
F
l
e
x
i
b
l
e
flowline
f
l
o
w
l
i
n
e
3
3
(*)
(
*
)
520
5
2
0
bar
b
a
r
Design
D
e
s
i
g
n
Pressure
P
r
e
s
s
u
r
e
for
f
o
r
flexible
f
l
e
x
i
b
l
e
jumper
j
u
m
p
e
r
(**)
(
*
*
)
205
2
0
5
bar
b
a
r
Water
W
a
t
e
r
depth
d
e
p
t
h
1200
1
2
0
0
mt
m
t
(*)Spare
(
*
)
S
p
a
r
e
11.5”
1
1
.
5
”
flexible
f
l
e
x
i
b
l
e
line
l
i
n
e
will
w
i
l
l
be
b
e
used
u
s
e
d
from
f
r
o
m
Merakes
M
e
r
a
k
e
s
Project.
P
r
o
j
e
c
t
.
(**)
(
*
*
)
Flexible
F
l
e
x
i
b
l
e
jumper
j
u
m
p
e
r
will
w
i
l
l
be
b
e
needed
n
e
e
d
e
d
to
t
o
connect
c
o
n
n
e
c
t
the
t
h
e
existing
e
x
i
s
t
i
n
g
JKK
J
K
K
manifold
m
a
n
i
f
o
l
d
1
1
with
w
i
t
h
the
t
h
e
new
n
e
w
FLET.
F
L
E
T
.
Use
U
s
e
of
o
f
flexible
f
l
e
x
i
b
l
e
solution
s
o
l
u
t
i
o
n
has
h
a
s
been
b
e
e
n
evaluated
e
v
a
l
u
a
t
e
d
during
d
u
r
i
n
g
the
t
h
e
concept
c
o
n
c
e
p
t
selection
s
e
l
e
c
t
i
o
n
phase
p
h
a
s
e
in
i
n
terms
t
e
r
m
s
of
o
f
mechanical
m
e
c
h
a
n
i
c
a
l
response
r
e
s
p
o
n
s
e
to
t
o
the
t
h
e
required
r
e
q
u
i
r
e
d
service
s
e
r
v
i
c
e
conditions
c
o
n
d
i
t
i
o
n
s
and
a
n
d
to
t
o
the
t
h
e
foreseen
f
o
r
e
s
e
e
n
water
w
a
t
e
r
depth.
d
e
p
t
h
.
Flexible
F
l
e
x
i
b
l
e
pipeline
p
i
p
e
l
i
n
e
has
h
a
s
been
b
e
e
n
also
a
l
s
o
compared
c
o
m
p
a
r
e
d
against
a
g
a
i
n
s
t
the
t
h
e
rigid
r
i
g
i
d
solution
s
o
l
u
t
i
o
n
in
i
n
terms
t
e
r
m
s
of
o
f
cost,
c
o
s
t
,
schedule
s
c
h
e
d
u
l
e
and
a
n
d
installability.
i
n
s
t
a
l
l
a
b
i
l
i
t
y
.
Flexible
F
l
e
x
i
b
l
e
jumpers
j
u
m
p
e
r
s
are
a
r
e
assumed
a
s
s
u
m
e
d
to
t
o
be
b
e
needed
n
e
e
d
e
d
also
a
l
s
o
between
b
e
t
w
e
e
n
2
2
and
a
n
d
4
4
wells
w
e
l
l
s
and
a
n
d
relevant
r
e
l
e
v
a
n
t
structure:
s
t
r
u
c
t
u
r
e
:
Flexible
F
l
e
x
i
b
l
e
Well
W
e
l
l
Jumper
J
u
m
p
e
r
Design
D
e
s
i
g
n
Pressure
P
r
e
s
s
u
r
e
520
5
2
0
bar
b
a
r
Flexible
F
l
e
x
i
b
l
e
Well
W
e
l
l
Jumper
J
u
m
p
e
r
Design
D
e
s
i
g
n
Temperature
T
e
m
p
e
r
a
t
u
r
e
70
7
0
°C
°
C
Flexible
F
l
e
x
i
b
l
e
Well
W
e
l
l
Jumper
J
u
m
p
e
r
Length
L
e
n
g
t
h
/
/
nr.
n
r
.
~90
~
9
0
mt
m
t
/
/
2
2
11
1
1
HEALTH,
H
E
A
L
T
H
,
SAFETY,
S
A
F
E
T
Y
,
ENVIRONMENT
E
N
V
I
R
O
N
M
E
N
T
The
T
h
e
project
p
r
o
j
e
c
t
is
i
s
developed
d
e
v
e
l
o
p
e
d
in
i
n
compliance
c
o
m
p
l
i
a
n
c
e
with
w
i
t
h
Indonesia
I
n
d
o
n
e
s
i
a
and
a
n
d
Upstream
U
p
s
t
r
e
a
m
HSE
H
S
E
policies,
p
o
l
i
c
i
e
s
,
referring
r
e
f
e
r
r
i
n
g
to
t
o
ISO
I
S
O
14001
1
4
0
0
1
requirements
r
e
q
u
i
r
e
m
e
n
t
s
for
f
o
r
Environmental
E
n
v
i
r
o
n
m
e
n
t
a
l
Management
M
a
n
a
g
e
m
e
n
t
Systems,
S
y
s
t
e
m
s
,
ISO
I
S
O
45001
4
5
0
0
1
and
a
n
d
OHSAS
O
H
S
A
S
18001
1
8
0
0
1
for
f
o
r
Occupational
O
c
c
u
p
a
t
i
o
n
a
l
Health
H
e
a
l
t
h
and
a
n
d
Safety
S
a
f
e
t
y
Management
M
a
n
a
g
e
m
e
n
t
Systems.
S
y
s
t
e
m
s
.
Indonesia
I
n
d
o
n
e
s
i
a
HSE
H
S
E
Policy
P
o
l
i
c
y
are
a
r
e
considered
c
o
n
s
i
d
e
r
e
d
as
a
s
the
t
h
e
reference
r
e
f
e
r
e
n
c
e
to
t
o
define
d
e
f
i
n
e
HSE
H
S
E
Project
P
r
o
j
e
c
t
Requirements
R
e
q
u
i
r
e
m
e
n
t
s
as
a
s
well
w
e
l
l
as
a
s
the
t
h
e
compliance
c
o
m
p
l
i
a
n
c
e
to
t
o
the
t
h
e
Upstream
U
p
s
t
r
e
a
m
Standards
S
t
a
n
d
a
r
d
s
and
a
n
d
10
1
0
HSE
H
S
E
policies.
p
o
l
i
c
i
e
s
.
HSE
H
S
E
design
d
e
s
i
g
n
criteria
c
r
i
t
e
r
i
a
to
t
o
be
b
e
applied
a
p
p
l
i
e
d
to
t
o
the
t
h
e
present
p
r
e
s
e
n
t
Concept
C
o
n
c
e
p
t
Definition
D
e
f
i
n
i
t
i
o
n
Phase
P
h
a
s
e
are
a
r
e
reported
r
e
p
o
r
t
e
d
in
i
n
the
t
h
e
preliminary
p
r
e
l
i
m
i
n
a
r
y
Health,
H
e
a
l
t
h
,
Safety
S
a
f
e
t
y
and
a
n
d
Environmental
E
n
v
i
r
o
n
m
e
n
t
a
l
(HSE)
(
H
S
E
)
Philosophy.
P
h
i
l
o
s
o
p
h
y
.
The
T
h
e
document
d
o
c
u
m
e
n
t
aims
a
i
m
s
to
t
o
ensure
e
n
s
u
r
e
an
a
n
inherently
i
n
h
e
r
e
n
t
l
y
safe
s
a
f
e
design,
d
e
s
i
g
n
,
in
i
n
order
o
r
d
e
r
to:
t
o
:
-
Minimize
M
i
n
i
m
i
z
e
the
t
h
e
potential
p
o
t
e
n
t
i
a
l
of
o
f
hazardous
h
a
z
a
r
d
o
u
s
occurrences;
o
c
c
u
r
r
e
n
c
e
s
;
-
Minimize
M
i
n
i
m
i
z
e
the
t
h
e
risk
r
i
s
k
and
a
n
d
consequences
c
o
n
s
e
q
u
e
n
c
e
s
of
o
f
an
a
n
accidental
a
c
c
i
d
e
n
t
a
l
event;
e
v
e
n
t
;
-
Ensure
E
n
s
u
r
e
a
a
safe
s
a
f
e
working
w
o
r
k
i
n
g
environment
e
n
v
i
r
o
n
m
e
n
t
for
f
o
r
personnel;
p
e
r
s
o
n
n
e
l
;
-
Ensure
E
n
s
u
r
e
adequate
a
d
e
q
u
a
t
e
means
m
e
a
n
s
of
o
f
escape
e
s
c
a
p
e
in
i
n
case
c
a
s
e
of
o
f
emergency;
e
m
e
r
g
e
n
c
y
;
-
Provide
P
r
o
v
i
d
e
sufficient
s
u
f
f
i
c
i
e
n
t
safety
s
a
f
e
t
y
devices
d
e
v
i
c
e
s
and
a
n
d
redundancy
r
e
d
u
n
d
a
n
c
y
to
t
o
detect,
d
e
t
e
c
t
,
isolate
i
s
o
l
a
t
e
and
a
n
d
minimize
m
i
n
i
m
i
z
e
uncontrolled
u
n
c
o
n
t
r
o
l
l
e
d
releases
r
e
l
e
a
s
e
s
of
o
f
flammable
f
l
a
m
m
a
b
l
e
and
a
n
d
toxic
t
o
x
i
c
fluids;
f
l
u
i
d
s
;
-
Provide
P
r
o
v
i
d
e
appropriate
a
p
p
r
o
p
r
i
a
t
e
fire
f
i
r
e
protection
p
r
o
t
e
c
t
i
o
n
systems
s
y
s
t
e
m
s
to
t
o
rapidly
r
a
p
i
d
l
y
bring
b
r
i
n
g
under
u
n
d
e
r
control
c
o
n
t
r
o
l
and
a
n
d
extinguish
e
x
t
i
n
g
u
i
s
h
any
a
n
y
reasonably
r
e
a
s
o
n
a
b
l
y
foreseeable
f
o
r
e
s
e
e
a
b
l
e
fire
f
i
r
e
which
w
h
i
c
h
could
c
o
u
l
d
develop
d
e
v
e
l
o
p
during
d
u
r
i
n
g
normal
n
o
r
m
a
l
operations;
o
p
e
r
a
t
i
o
n
s
;
-
Minimize
M
i
n
i
m
i
z
e
the
t
h
e
potential
p
o
t
e
n
t
i
a
l
pollution
p
o
l
l
u
t
i
o
n
of
o
f
the
t
h
e
environment.
e
n
v
i
r
o
n
m
e
n
t
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
The
T
h
e
project
p
r
o
j
e
c
t
development
d
e
v
e
l
o
p
m
e
n
t
shall
s
h
a
l
l
be
b
e
supported
s
u
p
p
o
r
t
e
d
by
b
y
an
a
n
HSE
H
S
E
design
d
e
s
i
g
n
based
b
a
s
e
d
on
o
n
a
a
formal
f
o
r
m
a
l
risk-based
r
i
s
k
-
b
a
s
e
d
assessment
a
s
s
e
s
s
m
e
n
t
process
p
r
o
c
e
s
s
(e.g.
(
e
.
g
.
HAZID,
H
A
Z
I
D
,
HAZOP,
H
A
Z
O
P
,
ESHIA,
E
S
H
I
A
,
other
o
t
h
e
r
safety
s
a
f
e
t
y
studies).
s
t
u
d
i
e
s
)
.
The
T
h
e
aim
a
i
m
of
o
f
the
t
h
e
formal
f
o
r
m
a
l
safety
s
a
f
e
t
y
assessment
a
s
s
e
s
s
m
e
n
t
process
p
r
o
c
e
s
s
is
i
s
to
t
o
ensure
e
n
s
u
r
e
that
t
h
a
t
all
a
l
l
potential
p
o
t
e
n
t
i
a
l
hazards
h
a
z
a
r
d
s
have
h
a
v
e
been
b
e
e
n
identified,
i
d
e
n
t
i
f
i
e
d
,
associated
a
s
s
o
c
i
a
t
e
d
risks
r
i
s
k
s
assessed,
a
s
s
e
s
s
e
d
,
and
a
n
d
measures
m
e
a
s
u
r
e
s
taken
t
a
k
e
n
to
t
o
eliminate,
e
l
i
m
i
n
a
t
e
,
reduce,
r
e
d
u
c
e
,
control
c
o
n
t
r
o
l
or
o
r
mitigate
m
i
t
i
g
a
t
e
the
t
h
e
consequences
c
o
n
s
e
q
u
e
n
c
e
s
of
o
f
those
t
h
o
s
e
hazards.
h
a
z
a
r
d
s
.
11.1
1
1
.
1
Safety
S
a
f
e
t
y
Criteria
C
r
i
t
e
r
i
a
The
T
h
e
objectives
o
b
j
e
c
t
i
v
e
s
of
o
f
the
t
h
e
HSE
H
S
E
Criteria
C
r
i
t
e
r
i
a
are
a
r
e
to:
t
o
:
-
minimise
m
i
n
i
m
i
s
e
the
t
h
e
risk
r
i
s
k
and
a
n
d
consequences
c
o
n
s
e
q
u
e
n
c
e
s
of
o
f
an
a
n
accidental
a
c
c
i
d
e
n
t
a
l
event;
e
v
e
n
t
;
-
minimise
m
i
n
i
m
i
s
e
the
t
h
e
potential
p
o
t
e
n
t
i
a
l
for
f
o
r
hazardous
h
a
z
a
r
d
o
u
s
occurrences;
o
c
c
u
r
r
e
n
c
e
s
;
-
maximise
m
a
x
i
m
i
s
e
the
t
h
e
benefits
b
e
n
e
f
i
t
s
of
o
f
protection
p
r
o
t
e
c
t
i
o
n
measures;
m
e
a
s
u
r
e
s
;
-
provide
p
r
o
v
i
d
e
sufficient
s
u
f
f
i
c
i
e
n
t
safety
s
a
f
e
t
y
devices
d
e
v
i
c
e
s
and
a
n
d
redundancy
r
e
d
u
n
d
a
n
c
y
to
t
o
isolate
i
s
o
l
a
t
e
and
a
n
d
minimise
m
i
n
i
m
i
s
e
uncontrolled
u
n
c
o
n
t
r
o
l
l
e
d
releases;
r
e
l
e
a
s
e
s
;
-
provide
p
r
o
v
i
d
e
appropriate
a
p
p
r
o
p
r
i
a
t
e
fire
f
i
r
e
protection
p
r
o
t
e
c
t
i
o
n
systems
s
y
s
t
e
m
s
to
t
o
control
c
o
n
t
r
o
l
any
a
n
y
reasonably
r
e
a
s
o
n
a
b
l
y
foreseeable
f
o
r
e
s
e
e
a
b
l
e
fire
f
i
r
e
which
w
h
i
c
h
could
c
o
u
l
d
develop
d
e
v
e
l
o
p
during
d
u
r
i
n
g
normal
n
o
r
m
a
l
operations;
o
p
e
r
a
t
i
o
n
s
;
-
ensure
e
n
s
u
r
e
adequate
a
d
e
q
u
a
t
e
means
m
e
a
n
s
of
o
f
escape
e
s
c
a
p
e
and
a
n
d
rescue
r
e
s
c
u
e
are
a
r
e
provided
p
r
o
v
i
d
e
d
from
f
r
o
m
all
a
l
l
areas;
a
r
e
a
s
;
-
minimise
m
i
n
i
m
i
s
e
the
t
h
e
potential
p
o
t
e
n
t
i
a
l
for
f
o
r
pollution
p
o
l
l
u
t
i
o
n
of
o
f
the
t
h
e
environment
e
n
v
i
r
o
n
m
e
n
t
from
f
r
o
m
accidental
a
c
c
i
d
e
n
t
a
l
spills,
s
p
i
l
l
s
,
venting
v
e
n
t
i
n
g
or
o
r
flaring
f
l
a
r
i
n
g
of
o
f
hazardous
h
a
z
a
r
d
o
u
s
materials;
m
a
t
e
r
i
a
l
s
;
-
ensure
e
n
s
u
r
e
that
t
h
a
t
all
a
l
l
operational
o
p
e
r
a
t
i
o
n
a
l
hazards
h
a
z
a
r
d
s
and
a
n
d
risks
r
i
s
k
s
are
a
r
e
minimised
m
i
n
i
m
i
s
e
d
during
d
u
r
i
n
g
construction
c
o
n
s
t
r
u
c
t
i
o
n
including
i
n
c
l
u
d
i
n
g
that
t
h
a
t
in
i
n
existing
e
x
i
s
t
i
n
g
plant.
p
l
a
n
t
.
The
T
h
e
goal
g
o
a
l
of
o
f
a
a
safe
s
a
f
e
facility
f
a
c
i
l
i
t
y
design
d
e
s
i
g
n
is
i
s
to
t
o
eliminate
e
l
i
m
i
n
a
t
e
the
t
h
e
high
h
i
g
h
(intolerable)
(
i
n
t
o
l
e
r
a
b
l
e
)
risks
r
i
s
k
s
and
a
n
d
to
t
o
reduce
r
e
d
u
c
e
the
t
h
e
medium
m
e
d
i
u
m
(tolerable)
(
t
o
l
e
r
a
b
l
e
)
risks
r
i
s
k
s
to
t
o
a
a
level
l
e
v
e
l
that
t
h
a
t
can
c
a
n
be
b
e
demonstrated
d
e
m
o
n
s
t
r
a
t
e
d
to
t
o
be
b
e
ALARP.
A
L
A
R
P
.
This
T
h
i
s
is
i
s
carried
c
a
r
r
i
e
d
out
o
u
t
by
b
y
reducing
r
e
d
u
c
i
n
g
the
t
h
e
probability
p
r
o
b
a
b
i
l
i
t
y
of
o
f
occurrence
o
c
c
u
r
r
e
n
c
e
of
o
f
events
e
v
e
n
t
s
and
a
n
d
minimizing
m
i
n
i
m
i
z
i
n
g
their
t
h
e
i
r
consequences.
c
o
n
s
e
q
u
e
n
c
e
s
.
The
T
h
e
main
m
a
i
n
principles
p
r
i
n
c
i
p
l
e
s
for
f
o
r
safe
s
a
f
e
facilities
f
a
c
i
l
i
t
i
e
s
design
d
e
s
i
g
n
and
a
n
d
operation
o
p
e
r
a
t
i
o
n
are:
a
r
e
:
-
support
s
u
p
p
o
r
t
for
f
o
r
design
d
e
s
i
g
n
decisions
d
e
c
i
s
i
o
n
s
making
m
a
k
i
n
g
based
b
a
s
e
d
on
o
n
sound
s
o
u
n
d
safety
s
a
f
e
t
y
reasoning;
r
e
a
s
o
n
i
n
g
;
-
containment
c
o
n
t
a
i
n
m
e
n
t
of
o
f
hydrocarbons
h
y
d
r
o
c
a
r
b
o
n
s
and
a
n
d
prevention
p
r
e
v
e
n
t
i
o
n
of
o
f
hydrocarbon
h
y
d
r
o
c
a
r
b
o
n
ignition;
i
g
n
i
t
i
o
n
;
-
minimization
m
i
n
i
m
i
z
a
t
i
o
n
of
o
f
the
t
h
e
chances
c
h
a
n
c
e
s
of
o
f
ignition;
i
g
n
i
t
i
o
n
;
-
prevention
p
r
e
v
e
n
t
i
o
n
of
o
f
fire
f
i
r
e
escalation
e
s
c
a
l
a
t
i
o
n
and
a
n
d
gas
g
a
s
monitoring;
m
o
n
i
t
o
r
i
n
g
;
-
provision
p
r
o
v
i
s
i
o
n
of
o
f
personnel
p
e
r
s
o
n
n
e
l
protection
p
r
o
t
e
c
t
i
o
n
and
a
n
d
escape.
e
s
c
a
p
e
.
11.2
1
1
.
2
Health
H
e
a
l
t
h
Considerations
C
o
n
s
i
d
e
r
a
t
i
o
n
s
The
T
h
e
Project
P
r
o
j
e
c
t
will
w
i
l
l
meet
m
e
e
t
the
t
h
e
health
h
e
a
l
t
h
and
a
n
d
regulatory
r
e
g
u
l
a
t
o
r
y
compliance
c
o
m
p
l
i
a
n
c
e
requirements
r
e
q
u
i
r
e
m
e
n
t
s
and
a
n
d
assure
a
s
s
u
r
e
the
t
h
e
appropriate
a
p
p
r
o
p
r
i
a
t
e
protection
p
r
o
t
e
c
t
i
o
n
of
o
f
worker
w
o
r
k
e
r
health
h
e
a
l
t
h
(employees
(
e
m
p
l
o
y
e
e
s
and
a
n
d
Contractors)
C
o
n
t
r
a
c
t
o
r
s
)
from
f
r
o
m
adverse
a
d
v
e
r
s
e
health
h
e
a
l
t
h
effects
e
f
f
e
c
t
s
that
t
h
a
t
may
m
a
y
result
r
e
s
u
l
t
from
f
r
o
m
the
t
h
e
design,
d
e
s
i
g
n
,
construction,
c
o
n
s
t
r
u
c
t
i
o
n
,
commissioning
c
o
m
m
i
s
s
i
o
n
i
n
g
and
a
n
d
operations
o
p
e
r
a
t
i
o
n
s
activities.
a
c
t
i
v
i
t
i
e
s
.
As
A
s
per
p
e
r
above,
a
b
o
v
e
,
the
t
h
e
health
h
e
a
l
t
h
related
r
e
l
a
t
e
d
risk
r
i
s
k
based
b
a
s
e
d
approach
a
p
p
r
o
a
c
h
will
w
i
l
l
include
i
n
c
l
u
d
e
the
t
h
e
following
f
o
l
l
o
w
i
n
g
objectives:
o
b
j
e
c
t
i
v
e
s
:
-
Identify
I
d
e
n
t
i
f
y
and
a
n
d
evaluate
e
v
a
l
u
a
t
e
health
h
e
a
l
t
h
hazards/risks
h
a
z
a
r
d
s
/
r
i
s
k
s
(e.g.,
(
e
.
g
.
,
occupational
o
c
c
u
p
a
t
i
o
n
a
l
health
h
e
a
l
t
h
risks
r
i
s
k
s
/
/
exposures,
e
x
p
o
s
u
r
e
s
,
vector-borne
v
e
c
t
o
r
-
b
o
r
n
e
disease,
d
i
s
e
a
s
e
,
infectious
i
n
f
e
c
t
i
o
u
s
disease,
d
i
s
e
a
s
e
,
accommodations,
a
c
c
o
m
m
o
d
a
t
i
o
n
s
,
food
f
o
o
d
and
a
n
d
water,
w
a
t
e
r
,
medical
m
e
d
i
c
a
l
support,
s
u
p
p
o
r
t
,
etc.).
e
t
c
.
)
.
-
Mitigate
M
i
t
i
g
a
t
e
health
h
e
a
l
t
h
hazards/risks.
h
a
z
a
r
d
s
/
r
i
s
k
s
.
-
Communicate
C
o
m
m
u
n
i
c
a
t
e
health
h
e
a
l
t
h
hazard/risk
h
a
z
a
r
d
/
r
i
s
k
information.
i
n
f
o
r
m
a
t
i
o
n
.
-
Define
D
e
f
i
n
e
staff
s
t
a
f
f
medical
m
e
d
i
c
a
l
fitness
f
i
t
n
e
s
s
for
f
o
r
duty
d
u
t
y
evaluation
e
v
a
l
u
a
t
i
o
n
programs.
p
r
o
g
r
a
m
s
.
-
Assess
A
s
s
e
s
s
health
h
e
a
l
t
h
of
o
f
potentially
p
o
t
e
n
t
i
a
l
l
y
exposed
e
x
p
o
s
e
d
workers.
w
o
r
k
e
r
s
.
-
Verify
V
e
r
i
f
y
satisfactory
s
a
t
i
s
f
a
c
t
o
r
y
health
h
e
a
l
t
h
management
m
a
n
a
g
e
m
e
n
t
through
t
h
r
o
u
g
h
health
h
e
a
l
t
h
inspections
i
n
s
p
e
c
t
i
o
n
s
and
a
n
d
surveillance
s
u
r
v
e
i
l
l
a
n
c
e
including
i
n
c
l
u
d
i
n
g
industrial
i
n
d
u
s
t
r
i
a
l
hygiene
h
y
g
i
e
n
e
management.
m
a
n
a
g
e
m
e
n
t
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
In
I
n
addition
a
d
d
i
t
i
o
n
to
t
o
the
t
h
e
Project
P
r
o
j
e
c
t
health
h
e
a
l
t
h
specifications
s
p
e
c
i
f
i
c
a
t
i
o
n
s
which
w
h
i
c
h
will
w
i
l
l
be
b
e
further
f
u
r
t
h
e
r
developed
d
e
v
e
l
o
p
e
d
during
d
u
r
i
n
g
the
t
h
e
next
n
e
x
t
Project
P
r
o
j
e
c
t
phase,
p
h
a
s
e
,
the
t
h
e
following
f
o
l
l
o
w
i
n
g
considerations,
c
o
n
s
i
d
e
r
a
t
i
o
n
s
,
and
a
n
d
not
n
o
t
limited
l
i
m
i
t
e
d
to,
t
o
,
shall
s
h
a
l
l
also
a
l
s
o
be
b
e
further
f
u
r
t
h
e
r
defined
d
e
f
i
n
e
d
and
a
n
d
incorporated
i
n
c
o
r
p
o
r
a
t
e
d
into
i
n
t
o
facility
f
a
c
i
l
i
t
y
design:
d
e
s
i
g
n
:
-
Facility
F
a
c
i
l
i
t
y
Noise
N
o
i
s
e
Sound
S
o
u
n
d
Level
L
e
v
e
l
Design
D
e
s
i
g
n
Criteria.
C
r
i
t
e
r
i
a
.
-
Medevac
M
e
d
e
v
a
c
arrangements.
a
r
r
a
n
g
e
m
e
n
t
s
.
-
Emergency
E
m
e
r
g
e
n
c
y
Shower
S
h
o
w
e
r
and
a
n
d
Eyewash
E
y
e
w
a
s
h
Facilities.
F
a
c
i
l
i
t
i
e
s
.
-
Design
D
e
s
i
g
n
of
o
f
Hazardous
H
a
z
a
r
d
o
u
s
Materials
M
a
t
e
r
i
a
l
s
Storage
S
t
o
r
a
g
e
and
a
n
d
Handling
H
a
n
d
l
i
n
g
Facility.
F
a
c
i
l
i
t
y
.
11.3
1
1
.
3
SIMOPS
S
I
M
O
P
S
Simultaneous
S
i
m
u
l
t
a
n
e
o
u
s
Operations
O
p
e
r
a
t
i
o
n
s
(SIMOPS)
(
S
I
M
O
P
S
)
refers
r
e
f
e
r
s
to
t
o
the
t
h
e
multiple
m
u
l
t
i
p
l
e
activities
a
c
t
i
v
i
t
i
e
s
such
s
u
c
h
as
a
s
continuous
c
o
n
t
i
n
u
o
u
s
production
p
r
o
d
u
c
t
i
o
n
of
o
f
hydrocarbons
h
y
d
r
o
c
a
r
b
o
n
s
(oil
(
o
i
l
or
o
r
gas),
g
a
s
)
,
executed
e
x
e
c
u
t
e
d
concurrently,
c
o
n
c
u
r
r
e
n
t
l
y
,
with
w
i
t
h
drilling,
d
r
i
l
l
i
n
g
,
maintenance,
m
a
i
n
t
e
n
a
n
c
e
,
construction,
c
o
n
s
t
r
u
c
t
i
o
n
,
commissioning
c
o
m
m
i
s
s
i
o
n
i
n
g
or
o
r
well
w
e
l
l
operations
o
p
e
r
a
t
i
o
n
s
in
i
n
any
a
n
y
existing
e
x
i
s
t
i
n
g
oil
o
i
l
and
a
n
d
gas
g
a
s
facility.
f
a
c
i
l
i
t
y
.
The
T
h
e
primary
p
r
i
m
a
r
y
benefits
b
e
n
e
f
i
t
s
of
o
f
carrying
c
a
r
r
y
i
n
g
out
o
u
t
simultaneous
s
i
m
u
l
t
a
n
e
o
u
s
operations
o
p
e
r
a
t
i
o
n
s
whilst
w
h
i
l
s
t
maintaining
m
a
i
n
t
a
i
n
i
n
g
production
p
r
o
d
u
c
t
i
o
n
are
a
r
e
the
t
h
e
economic
e
c
o
n
o
m
i
c
incentives
i
n
c
e
n
t
i
v
e
s
within
w
i
t
h
i
n
controllable
c
o
n
t
r
o
l
l
a
b
l
e
risk,
r
i
s
k
,
thus
t
h
u
s
minimising
m
i
n
i
m
i
s
i
n
g
the
t
h
e
deferment
d
e
f
e
r
m
e
n
t
of
o
f
hydrocarbon
h
y
d
r
o
c
a
r
b
o
n
production.
p
r
o
d
u
c
t
i
o
n
.
The
T
h
e
interaction
i
n
t
e
r
a
c
t
i
o
n
between
b
e
t
w
e
e
n
the
t
h
e
multiple
m
u
l
t
i
p
l
e
activities
a
c
t
i
v
i
t
i
e
s
tends
t
e
n
d
s
to
t
o
result
r
e
s
u
l
t
in
i
n
an
a
n
increased
i
n
c
r
e
a
s
e
d
operational
o
p
e
r
a
t
i
o
n
a
l
complexity
c
o
m
p
l
e
x
i
t
y
and
a
n
d
higher
h
i
g
h
e
r
level
l
e
v
e
l
of
o
f
risk.
r
i
s
k
.
This
T
h
i
s
is
i
s
because
b
e
c
a
u
s
e
during
d
u
r
i
n
g
each
e
a
c
h
SIMOPS,
S
I
M
O
P
S
,
more
m
o
r
e
than
t
h
a
n
one
o
n
e
activity
a
c
t
i
v
i
t
y
being
b
e
i
n
g
conducted
c
o
n
d
u
c
t
e
d
concurrently
c
o
n
c
u
r
r
e
n
t
l
y
may
m
a
y
result
r
e
s
u
l
t
in
i
n
the
t
h
e
introduction
i
n
t
r
o
d
u
c
t
i
o
n
of
o
f
additional
a
d
d
i
t
i
o
n
a
l
risk
r
i
s
k
and
a
n
d
increased
i
n
c
r
e
a
s
e
d
probability
p
r
o
b
a
b
i
l
i
t
y
of
o
f
failure
f
a
i
l
u
r
e
to
t
o
control
c
o
n
t
r
o
l
the
t
h
e
hazard
h
a
z
a
r
d
associated
a
s
s
o
c
i
a
t
e
d
with
w
i
t
h
these
t
h
e
s
e
risks.
r
i
s
k
s
.
For
F
o
r
example,
e
x
a
m
p
l
e
,
presence
p
r
e
s
e
n
c
e
of
o
f
additional
a
d
d
i
t
i
o
n
a
l
ignition
i
g
n
i
t
i
o
n
sources
s
o
u
r
c
e
s
from
f
r
o
m
hot
h
o
t
work
w
o
r
k
activities
a
c
t
i
v
i
t
i
e
s
such
s
u
c
h
as
a
s
cutting,
c
u
t
t
i
n
g
,
welding,
w
e
l
d
i
n
g
,
etc.,
e
t
c
.
,
would
w
o
u
l
d
increase
i
n
c
r
e
a
s
e
the
t
h
e
probability
p
r
o
b
a
b
i
l
i
t
y
of
o
f
ignition
i
g
n
i
t
i
o
n
should
s
h
o
u
l
d
there
t
h
e
r
e
be
b
e
a
a
hydrocarbon
h
y
d
r
o
c
a
r
b
o
n
leak
l
e
a
k
on
o
n
the
t
h
e
process
p
r
o
c
e
s
s
facility
f
a
c
i
l
i
t
y
nearby.
n
e
a
r
b
y
.
11.4
1
1
.
4
RISK
R
I
S
K
IDENTIFICATION
I
D
E
N
T
I
F
I
C
A
T
I
O
N
During
D
u
r
i
n
g
current
c
u
r
r
e
n
t
Project
P
r
o
j
e
c
t
Phase
P
h
a
s
e
the
t
h
e
following
f
o
l
l
o
w
i
n
g
studies
s
t
u
d
i
e
s
will
w
i
l
l
be
b
e
carried
c
a
r
r
i
e
d
on:
o
n
:
-
-
HAZID
H
A
Z
I
D
Analisys:
A
n
a
l
i
s
y
s
:
HAZID
H
A
Z
I
D
is
i
s
a
a
structured
s
t
r
u
c
t
u
r
e
d
review
r
e
v
i
e
w
technique
t
e
c
h
n
i
q
u
e
for
f
o
r
the
t
h
e
early
e
a
r
l
y
identification
i
d
e
n
t
i
f
i
c
a
t
i
o
n
of
o
f
all
a
l
l
significant
s
i
g
n
i
f
i
c
a
n
t
hazards
h
a
z
a
r
d
s
associated
a
s
s
o
c
i
a
t
e
d
with
w
i
t
h
the
t
h
e
particular
p
a
r
t
i
c
u
l
a
r
activity
a
c
t
i
v
i
t
y
under
u
n
d
e
r
consideration.
c
o
n
s
i
d
e
r
a
t
i
o
n
.
HAZID
H
A
Z
I
D
is
i
s
carried
c
a
r
r
i
e
d
out
o
u
t
by
b
y
a
a
systematic
s
y
s
t
e
m
a
t
i
c
analysis
a
n
a
l
y
s
i
s
of
o
f
all
a
l
l
the
t
h
e
potential
p
o
t
e
n
t
i
a
l
external
e
x
t
e
r
n
a
l
threats
t
h
r
e
a
t
s
with
w
i
t
h
the
t
h
e
potential
p
o
t
e
n
t
i
a
l
to
t
o
generate
g
e
n
e
r
a
t
e
health,
h
e
a
l
t
h
,
safety,
s
a
f
e
t
y
,
environmental,
e
n
v
i
r
o
n
m
e
n
t
a
l
,
asset
a
s
s
e
t
and
a
n
d
reputational
r
e
p
u
t
a
t
i
o
n
a
l
risks.
r
i
s
k
s
.
-
-
HAZOP
H
A
Z
O
P
Analisys:
A
n
a
l
i
s
y
s
:
HAZOP
H
A
Z
O
P
studies
s
t
u
d
i
e
s
shall
s
h
a
l
l
be
b
e
used
u
s
e
d
to
t
o
analyze
a
n
a
l
y
z
e
the
t
h
e
design
d
e
s
i
g
n
of
o
f
operating
o
p
e
r
a
t
i
n
g
facilities,
f
a
c
i
l
i
t
i
e
s
,
new
n
e
w
facilities
f
a
c
i
l
i
t
i
e
s
or
o
r
modifications
m
o
d
i
f
i
c
a
t
i
o
n
s
to
t
o
process
p
r
o
c
e
s
s
and
a
n
d
utility
u
t
i
l
i
t
y
systems
s
y
s
t
e
m
s
as
a
s
a
a
way
w
a
y
of
o
f
rigorously
r
i
g
o
r
o
u
s
l
y
and
a
n
d
systematically
s
y
s
t
e
m
a
t
i
c
a
l
l
y
checking
c
h
e
c
k
i
n
g
the
t
h
e
design
d
e
s
i
g
n
for
f
o
r
safety,
s
a
f
e
t
y
,
operability
o
p
e
r
a
b
i
l
i
t
y
and
a
n
d
conformity
c
o
n
f
o
r
m
i
t
y
with
w
i
t
h
codes
c
o
d
e
s
of
o
f
practice.
p
r
a
c
t
i
c
e
.
All
A
l
l
these
t
h
e
s
e
sessions
s
e
s
s
i
o
n
s
have
h
a
v
e
the
t
h
e
aim
a
i
m
to
t
o
identify
i
d
e
n
t
i
f
y
as
a
s
soon
s
o
o
n
as
a
s
possible
p
o
s
s
i
b
l
e
all
a
l
l
risks
r
i
s
k
s
associated
a
s
s
o
c
i
a
t
e
d
to
t
o
the
t
h
e
production
p
r
o
d
u
c
t
i
o
n
phase
p
h
a
s
e
that
t
h
a
t
can
c
a
n
have
h
a
v
e
impact
i
m
p
a
c
t
principally
p
r
i
n
c
i
p
a
l
l
y
on
o
n
Safety,
S
a
f
e
t
y
,
Environmental
E
n
v
i
r
o
n
m
e
n
t
a
l
and
a
n
d
Asset.
A
s
s
e
t
.
Risk
R
i
s
k
matrix
m
a
t
r
i
x
that
t
h
a
t
will
w
i
l
l
be
b
e
used
u
s
e
d
for
f
o
r
risk
r
i
s
k
ranking
r
a
n
k
i
n
g
(when
(
w
h
e
n
required)
r
e
q
u
i
r
e
d
)
as
a
s
reported
r
e
p
o
r
t
e
d
below:
b
e
l
o
w
:
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Table
T
a
b
l
e
21:
2
1
:
Basic
B
a
s
i
c
risk
r
i
s
k
matrix
m
a
t
r
i
x
(full
(
f
u
l
l
qualitative
q
u
a
l
i
t
a
t
i
v
e
approach)
a
p
p
r
o
a
c
h
)
All
A
l
l
reccomendations
r
e
c
c
o
m
e
n
d
a
t
i
o
n
s
arisen
a
r
i
s
e
n
during
d
u
r
i
n
g
sessions
s
e
s
s
i
o
n
s
will
w
i
l
l
generate
g
e
n
e
r
a
t
e
an
a
n
action
a
c
t
i
o
n
that
t
h
a
t
will
w
i
l
l
be
b
e
in
i
n
charge
c
h
a
r
g
e
to
t
o
the
t
h
e
dedicated
d
e
d
i
c
a
t
e
d
department.
d
e
p
a
r
t
m
e
n
t
.
All
A
l
l
actions
a
c
t
i
o
n
s
shall
s
h
a
l
l
be
b
e
correctly
c
o
r
r
e
c
t
l
y
managed
m
a
n
a
g
e
d
before
b
e
f
o
r
e
the
t
h
e
end
e
n
d
of
o
f
current
c
u
r
r
e
n
t
Project
P
r
o
j
e
c
t
phase,
p
h
a
s
e
,
with
w
i
t
h
evidence
e
v
i
d
e
n
c
e
of
o
f
their
t
h
e
i
r
implementation.
i
m
p
l
e
m
e
n
t
a
t
i
o
n
.
11.5
1
1
.
5
Environmental,
E
n
v
i
r
o
n
m
e
n
t
a
l
,
Social
S
o
c
i
a
l
and
a
n
d
Health
H
e
a
l
t
h
Impact
I
m
p
a
c
t
Assessment
A
s
s
e
s
s
m
e
n
t
During
D
u
r
i
n
g
FEED
F
E
E
D
Project
P
r
o
j
e
c
t
phase
p
h
a
s
e
a
a
Environmental,
E
n
v
i
r
o
n
m
e
n
t
a
l
,
Social
S
o
c
i
a
l
and
a
n
d
Health
H
e
a
l
t
h
Impact
I
m
p
a
c
t
Assessment
A
s
s
e
s
s
m
e
n
t
SoW
S
o
W
has
h
a
s
been
b
e
e
n
produced.
p
r
o
d
u
c
e
d
.
The
T
h
e
outcomes
o
u
t
c
o
m
e
s
of
o
f
the
t
h
e
study
s
t
u
d
y
will
w
i
l
l
be
b
e
shared
s
h
a
r
e
d
with
w
i
t
h
Contractor
C
o
n
t
r
a
c
t
o
r
for
f
o
r
design
d
e
s
i
g
n
purposes.
p
u
r
p
o
s
e
s
.
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
12
1
2
GHG
G
H
G
EMISSION
E
M
I
S
S
I
O
N
AND
A
N
D
MITIGATION
M
I
T
I
G
A
T
I
O
N
OF
O
F
CLIMATE
C
L
I
M
A
T
E
CHANGE
C
H
A
N
G
E
EFFECTS:
E
F
F
E
C
T
S
:
The
T
h
e
Company
C
o
m
p
a
n
y
has
h
a
s
a
a
strong
s
t
r
o
n
g
commitment
c
o
m
m
i
t
m
e
n
t
to
t
o
reduce
r
e
d
u
c
e
GHG
G
H
G
emissions
e
m
i
s
s
i
o
n
s
in
i
n
business
b
u
s
i
n
e
s
s
initiatives:
i
n
i
t
i
a
t
i
v
e
s
:
the
t
h
e
impact
i
m
p
a
c
t
shall
s
h
a
l
l
be
b
e
minimized
m
i
n
i
m
i
z
e
d
deploying
d
e
p
l
o
y
i
n
g
proper
p
r
o
p
e
r
technologies
t
e
c
h
n
o
l
o
g
i
e
s
and
a
n
d
taking
t
a
k
i
n
g
into
i
n
t
o
account
a
c
c
o
u
n
t
an
a
n
optimization
o
p
t
i
m
i
z
a
t
i
o
n
on
o
n
the
t
h
e
overall
o
v
e
r
a
l
l
project
p
r
o
j
e
c
t
production
p
r
o
d
u
c
t
i
o
n
life.
l
i
f
e
.
This
T
h
i
s
shall
s
h
a
l
l
be
b
e
achieved
a
c
h
i
e
v
e
d
through
t
h
r
o
u
g
h
appropriate
a
p
p
r
o
p
r
i
a
t
e
measures,
m
e
a
s
u
r
e
s
,
depending
d
e
p
e
n
d
i
n
g
on
o
n
the
t
h
e
specific
s
p
e
c
i
f
i
c
project
p
r
o
j
e
c
t
characteristics.
c
h
a
r
a
c
t
e
r
i
s
t
i
c
s
.
In
I
n
particular:
p
a
r
t
i
c
u
l
a
r
:
-
No
N
o
routine
r
o
u
t
i
n
e
flaring
f
l
a
r
i
n
g
is
i
s
allowed
a
l
l
o
w
e
d
at
a
t
any
a
n
y
stage
s
t
a
g
e
of
o
f
the
t
h
e
project.
p
r
o
j
e
c
t
.
-
Non-routine
N
o
n
-
r
o
u
t
i
n
e
flaring
f
l
a
r
i
n
g
shall
s
h
a
l
l
be
b
e
minimized.
m
i
n
i
m
i
z
e
d
.
-
Metering
M
e
t
e
r
i
n
g
systems
s
y
s
t
e
m
s
shall
s
h
a
l
l
be
b
e
installed
i
n
s
t
a
l
l
e
d
for
f
o
r
all
a
l
l
gas
g
a
s
streams.
s
t
r
e
a
m
s
.
-
Continuous
C
o
n
t
i
n
u
o
u
s
CO2
C
O
2
venting
v
e
n
t
i
n
g
from
f
r
o
m
fluids
f
l
u
i
d
s
nor
n
o
r
Methane
M
e
t
h
a
n
e
venting
v
e
n
t
i
n
g
contained
c
o
n
t
a
i
n
e
d
is
i
s
allowed
a
l
l
o
w
e
d
at
a
t
any
a
n
y
time
t
i
m
e
of
o
f
production.
p
r
o
d
u
c
t
i
o
n
.
-
Stationary
S
t
a
t
i
o
n
a
r
y
combustion
c
o
m
b
u
s
t
i
o
n
emissions
e
m
i
s
s
i
o
n
s
shall
s
h
a
l
l
be
b
e
minimized
m
i
n
i
m
i
z
e
d
always
a
l
w
a
y
s
preferring
p
r
e
f
e
r
r
i
n
g
low
l
o
w
energy
e
n
e
r
g
y
intensity
i
n
t
e
n
s
i
t
y
processes
p
r
o
c
e
s
s
e
s
and
a
n
d
deploying
d
e
p
l
o
y
i
n
g
high
h
i
g
h
efficiency
e
f
f
i
c
i
e
n
c
y
fuel
f
u
e
l
gas-based
g
a
s
-
b
a
s
e
d
power
p
o
w
e
r
generation
g
e
n
e
r
a
t
i
o
n
systems
s
y
s
t
e
m
s
or
o
r
evaluating
e
v
a
l
u
a
t
i
n
g
connection
c
o
n
n
e
c
t
i
o
n
to
t
o
local
l
o
c
a
l
power
p
o
w
e
r
network
n
e
t
w
o
r
k
where
w
h
e
r
e
feasible.
f
e
a
s
i
b
l
e
.
12.1
1
2
.
1
Water
W
a
t
e
r
Management
M
a
n
a
g
e
m
e
n
t
The
T
h
e
minimum
m
i
n
i
m
u
m
general
g
e
n
e
r
a
l
requirements
r
e
q
u
i
r
e
m
e
n
t
s
to
t
o
be
b
e
adhered
a
d
h
e
r
e
d
to
t
o
are
a
r
e
as
a
s
follows:
f
o
l
l
o
w
s
:
-
Reduction
R
e
d
u
c
t
i
o
n
of
o
f
the
t
h
e
usage
u
s
a
g
e
of
o
f
water
w
a
t
e
r
shall
s
h
a
l
l
represent
r
e
p
r
e
s
e
n
t
one
o
n
e
of
o
f
the
t
h
e
main
m
a
i
n
design
d
e
s
i
g
n
criteria.
c
r
i
t
e
r
i
a
.
Water
W
a
t
e
r
re-use
r
e
-
u
s
e
shall
s
h
a
l
l
be
b
e
preferable
p
r
e
f
e
r
a
b
l
e
to
t
o
recycle.
r
e
c
y
c
l
e
.
Water
W
a
t
e
r
recycle
r
e
c
y
c
l
e
shall
s
h
a
l
l
be
b
e
preferable
p
r
e
f
e
r
a
b
l
e
to
t
o
water
w
a
t
e
r
discharge.
d
i
s
c
h
a
r
g
e
.
-
Installation
I
n
s
t
a
l
l
a
t
i
o
n
of
o
f
flow
f
l
o
w
meters
m
e
t
e
r
s
for
f
o
r
each
e
a
c
h
water
w
a
t
e
r
stream
s
t
r
e
a
m
(input
(
i
n
p
u
t
and
a
n
d
output)
o
u
t
p
u
t
)
shall
s
h
a
l
l
be
b
e
assured.
a
s
s
u
r
e
d
.
Any
A
n
y
discharge
d
i
s
c
h
a
r
g
e
of
o
f
water
w
a
t
e
r
brought
b
r
o
u
g
h
t
into
i
n
t
o
contact
c
o
n
t
a
c
t
with
w
i
t
h
hydrocarbons,
h
y
d
r
o
c
a
r
b
o
n
s
,
chemicals,
c
h
e
m
i
c
a
l
s
,
and
a
n
d
any
a
n
y
potential
p
o
t
e
n
t
i
a
l
source
s
o
u
r
c
e
of
o
f
contamination
c
o
n
t
a
m
i
n
a
t
i
o
n
shall
s
h
a
l
l
be
b
e
routed
r
o
u
t
e
d
to
t
o
treatment
t
r
e
a
t
m
e
n
t
system
s
y
s
t
e
m
before
b
e
f
o
r
e
final
f
i
n
a
l
disposal.
d
i
s
p
o
s
a
l
.
13
1
3
REGULARITY
R
E
G
U
L
A
R
I
T
Y
AND
A
N
D
OPERATION
O
P
E
R
A
T
I
O
N
The
T
h
e
Regularity
R
e
g
u
l
a
r
i
t
y
and
a
n
d
operation
o
p
e
r
a
t
i
o
n
principles
p
r
i
n
c
i
p
l
e
s
of
o
f
Development
D
e
v
e
l
o
p
m
e
n
t
Project
P
r
o
j
e
c
t
aim
a
i
m
at
a
t
ensuring
e
n
s
u
r
i
n
g
uninterrupted
u
n
i
n
t
e
r
r
u
p
t
e
d
exploitation
e
x
p
l
o
i
t
a
t
i
o
n
operations,
o
p
e
r
a
t
i
o
n
s
,
maximizing
m
a
x
i
m
i
z
i
n
g
the
t
h
e
ergonomics
e
r
g
o
n
o
m
i
c
s
of
o
f
installation
i
n
s
t
a
l
l
a
t
i
o
n
and
a
n
d
minimizing
m
i
n
i
m
i
z
i
n
g
operation
o
p
e
r
a
t
i
o
n
life-
l
i
f
e
-
cycle
c
y
c
l
e
cost,
c
o
s
t
,
assuring
a
s
s
u
r
i
n
g
the
t
h
e
asset
a
s
s
e
t
integrity,
i
n
t
e
g
r
i
t
y
,
reducing
r
e
d
u
c
i
n
g
the
t
h
e
risk
r
i
s
k
of
o
f
accident
a
c
c
i
d
e
n
t
occurrence,
o
c
c
u
r
r
e
n
c
e
,
minimizing
m
i
n
i
m
i
z
i
n
g
worker
w
o
r
k
e
r
exposure
e
x
p
o
s
u
r
e
to
t
o
risks
r
i
s
k
s
and
a
n
d
protecting
p
r
o
t
e
c
t
i
n
g
the
t
h
e
environment.
e
n
v
i
r
o
n
m
e
n
t
.
The
T
h
e
assurance
a
s
s
u
r
a
n
c
e
will
w
i
l
l
be
b
e
achieved
a
c
h
i
e
v
e
d
by
b
y
having
h
a
v
i
n
g
in
i
n
place
p
l
a
c
e
appropriate
a
p
p
r
o
p
r
i
a
t
e
management
m
a
n
a
g
e
m
e
n
t
control
c
o
n
t
r
o
l
and
a
n
d
engineering
e
n
g
i
n
e
e
r
i
n
g
practices
p
r
a
c
t
i
c
e
s
that
t
h
a
t
meet
m
e
e
t
the
t
h
e
requirements
r
e
q
u
i
r
e
m
e
n
t
s
of
o
f
the
t
h
e
Company,
C
o
m
p
a
n
y
,
international
i
n
t
e
r
n
a
t
i
o
n
a
l
standards
s
t
a
n
d
a
r
d
s
and
a
n
d
legal
l
e
g
a
l
obligations
o
b
l
i
g
a
t
i
o
n
s
and
a
n
d
any
a
n
y
other
o
t
h
e
r
applicable
a
p
p
l
i
c
a
b
l
e
national
n
a
t
i
o
n
a
l
regulation
r
e
g
u
l
a
t
i
o
n
(see
(
s
e
e
also
a
l
s
o
ref.
r
e
f
.
[3]).
[
3
]
)
.
Asset
A
s
s
e
t
Life
L
i
f
e
Cycle
C
y
c
l
e
processes
p
r
o
c
e
s
s
e
s
will
w
i
l
l
be
b
e
formalized
f
o
r
m
a
l
i
z
e
d
in
i
n
Development
D
e
v
e
l
o
p
m
e
n
t
Management
M
a
n
a
g
e
m
e
n
t
System
S
y
s
t
e
m
(DMS)
(
D
M
S
)
and
a
n
d
Operation
O
p
e
r
a
t
i
o
n
Management
M
a
n
a
g
e
m
e
n
t
System
S
y
s
t
e
m
(OMS),
(
O
M
S
)
,
providing
p
r
o
v
i
d
i
n
g
directions
d
i
r
e
c
t
i
o
n
s
and
a
n
d
requirements
r
e
q
u
i
r
e
m
e
n
t
s
for
f
o
r
all
a
l
l
those
t
h
o
s
e
activities
a
c
t
i
v
i
t
i
e
s
of
o
f
Development
D
e
v
e
l
o
p
m
e
n
t
and
a
n
d
Production
P
r
o
d
u
c
t
i
o
n
processes
p
r
o
c
e
s
s
e
s
involving
i
n
v
o
l
v
i
n
g
Indonesia.
I
n
d
o
n
e
s
i
a
.
The
T
h
e
FPU
F
P
U
will
w
i
l
l
be
b
e
permanently
p
e
r
m
a
n
e
n
t
l
y
manned
m
a
n
n
e
d
while
w
h
i
l
e
a
a
non
n
o
n
continuous
c
o
n
t
i
n
u
o
u
s
presence
p
r
e
s
e
n
c
e
of
o
f
workers
w
o
r
k
e
r
s
is
i
s
foreseen
f
o
r
e
s
e
e
n
for
f
o
r
the
t
h
e
onshore
o
n
s
h
o
r
e
facilities
f
a
c
i
l
i
t
i
e
s
(i.e.
(
i
.
e
.
unattended
u
n
a
t
t
e
n
d
e
d
operations).
o
p
e
r
a
t
i
o
n
s
)
.
The
T
h
e
staff
s
t
a
f
f
onboard
o
n
b
o
a
r
d
the
t
h
e
FPU
F
P
U
will
w
i
l
l
operate
o
p
e
r
a
t
e
in
i
n
turning
t
u
r
n
i
n
g
shifts
s
h
i
f
t
s
and
a
n
d
will
w
i
l
l
be
b
e
accommodated
a
c
c
o
m
m
o
d
a
t
e
d
in
i
n
the
t
h
e
LQ
L
Q
module
m
o
d
u
l
e
that
t
h
a
t
will
w
i
l
l
include
i
n
c
l
u
d
e
living
l
i
v
i
n
g
room,
r
o
o
m
,
recreation
r
e
c
r
e
a
t
i
o
n
room,
r
o
o
m
,
first
f
i
r
s
t
aid
a
i
d
facilities
f
a
c
i
l
i
t
i
e
s
and
a
n
d
a
a
Helideck.
H
e
l
i
d
e
c
k
.
In
I
n
order
o
r
d
e
r
to
t
o
optimize
o
p
t
i
m
i
z
e
the
t
h
e
levels
l
e
v
e
l
s
of
o
f
the
t
h
e
manning
m
a
n
n
i
n
g
commensurate
c
o
m
m
e
n
s
u
r
a
t
e
with
w
i
t
h
the
t
h
e
control
c
o
n
t
r
o
l
technology
t
e
c
h
n
o
l
o
g
y
adopted,
a
d
o
p
t
e
d
,
the
t
h
e
following
f
o
l
l
o
w
i
n
g
criteria
c
r
i
t
e
r
i
a
will
w
i
l
l
be
b
e
implemented:
i
m
p
l
e
m
e
n
t
e
d
:
-
Utilize
U
t
i
l
i
z
e
support
s
u
p
p
o
r
t
infrastructure
i
n
f
r
a
s
t
r
u
c
t
u
r
e
to
t
o
manage
m
a
n
a
g
e
staffing
s
t
a
f
f
i
n
g
levels
l
e
v
e
l
s
synergies;
s
y
n
e
r
g
i
e
s
;
-
Ensure
E
n
s
u
r
e
high
h
i
g
h
levels
l
e
v
e
l
s
of
o
f
staff
s
t
a
f
f
competence
c
o
m
p
e
t
e
n
c
e
in
i
n
all
a
l
l
teams;
t
e
a
m
s
;
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
-
Adopt
A
d
o
p
t
empowerment
e
m
p
o
w
e
r
m
e
n
t
approach
a
p
p
r
o
a
c
h
to
t
o
work;
w
o
r
k
;
-
Adopt
A
d
o
p
t
suitable
s
u
i
t
a
b
l
e
staff
s
t
a
f
f
competence
c
o
m
p
e
t
e
n
c
e
assurance
a
s
s
u
r
a
n
c
e
and
a
n
d
development
d
e
v
e
l
o
p
m
e
n
t
methods;
m
e
t
h
o
d
s
;
-
Implement
I
m
p
l
e
m
e
n
t
a
a
contracting
c
o
n
t
r
a
c
t
i
n
g
plan
p
l
a
n
aimed
a
i
m
e
d
to
t
o
supplement
s
u
p
p
l
e
m
e
n
t
staffing
s
t
a
f
f
i
n
g
needs
n
e
e
d
s
with
w
i
t
h
external
e
x
t
e
r
n
a
l
technical
t
e
c
h
n
i
c
a
l
sources;
s
o
u
r
c
e
s
;
-
Take
T
a
k
e
into
i
n
t
o
consideration
c
o
n
s
i
d
e
r
a
t
i
o
n
the
t
h
e
local
l
o
c
a
l
content
c
o
n
t
e
n
t
requirements.
r
e
q
u
i
r
e
m
e
n
t
s
.
14
1
4
SIMOPS
S
I
M
O
P
S
AND
A
N
D
CONOPS
C
O
N
O
P
S
REQUIREMENTS
R
E
Q
U
I
R
E
M
E
N
T
S
In
I
n
this
t
h
i
s
chapter
c
h
a
p
t
e
r
all
a
l
l
the
t
h
e
specific
s
p
e
c
i
f
i
c
requirements
r
e
q
u
i
r
e
m
e
n
t
s
for
f
o
r
SIMOPS
S
I
M
O
P
S
and
a
n
d
CONOPS
C
O
N
O
P
S
coming
c
o
m
i
n
g
from
f
r
o
m
the
t
h
e
development/project
d
e
v
e
l
o
p
m
e
n
t
/
p
r
o
j
e
c
t
within
w
i
t
h
i
n
or
o
r
nearby
n
e
a
r
b
y
existing
e
x
i
s
t
i
n
g
or
o
r
operating
o
p
e
r
a
t
i
n
g
facilities
f
a
c
i
l
i
t
i
e
s
or
o
r
nearby
n
e
a
r
b
y
other
o
t
h
e
r
operations.
o
p
e
r
a
t
i
o
n
s
.
SIMOPS
S
I
M
O
P
S
It
I
t
is
i
s
preliminary
p
r
e
l
i
m
i
n
a
r
y
considered
c
o
n
s
i
d
e
r
e
d
that
t
h
a
t
during
d
u
r
i
n
g
the
t
h
e
installation
i
n
s
t
a
l
l
a
t
i
o
n
activities
a
c
t
i
v
i
t
i
e
s
of
o
f
EPCI
E
P
C
I
facilities
f
a
c
i
l
i
t
i
e
s
there
t
h
e
r
e
is
i
s
a
a
risk
r
i
s
k
that
t
h
a
t
the
t
h
e
following
f
o
l
l
o
w
i
n
g
activities
a
c
t
i
v
i
t
i
e
s
may
m
a
y
be
b
e
accomplished
a
c
c
o
m
p
l
i
s
h
e
d
simultaneously:
s
i
m
u
l
t
a
n
e
o
u
s
l
y
:
-
Drilling
D
r
i
l
l
i
n
g
and
a
n
d
completion
c
o
m
p
l
e
t
i
o
n
activities
a
c
t
i
v
i
t
i
e
s
-
Produciton
P
r
o
d
u
c
i
t
o
n
from
f
r
o
m
facilities
f
a
c
i
l
i
t
i
e
s
already
a
l
r
e
a
d
y
handed
h
a
n
d
e
d
over
o
v
e
r
to
t
o
Company.
C
o
m
p
a
n
y
.
CONOPS
C
O
N
O
P
S
It
I
t
is
i
s
preliminary
p
r
e
l
i
m
i
n
a
r
y
assumed
a
s
s
u
m
e
d
that
t
h
a
t
any
a
n
y
FPU
F
P
U
activty
a
c
t
i
v
t
y
under
u
n
d
e
r
EPCI
E
P
C
I
scope
s
c
o
p
e
will
w
i
l
l
be
b
e
performed
p
e
r
f
o
r
m
e
d
simultaneously
s
i
m
u
l
t
a
n
e
o
u
s
l
y
with
w
i
t
h
FPU
F
P
U
production.
p
r
o
d
u
c
t
i
o
n
.
Further
F
u
r
t
h
e
r
analysis
a
n
a
l
y
s
i
s
will
w
i
l
l
be
b
e
made
m
a
d
e
to
t
o
deeper
d
e
e
p
e
r
comprehend
c
o
m
p
r
e
h
e
n
d
the
t
h
e
criticality
c
r
i
t
i
c
a
l
i
t
y
and
a
n
d
the
t
h
e
advantages
a
d
v
a
n
t
a
g
e
s
of
o
f
this
t
h
i
s
solution
s
o
l
u
t
i
o
n
and
a
n
d
eventually
e
v
e
n
t
u
a
l
l
y
propose
p
r
o
p
o
s
e
alternative
a
l
t
e
r
n
a
t
i
v
e
options.
o
p
t
i
o
n
s
.
15
1
5
ATTACHMENTS
A
T
T
A
C
H
M
E
N
T
S
Annex
A
n
n
e
x
1
1
–
–
Limits
L
i
m
i
t
s
and
a
n
d
Quality
Q
u
a
l
i
t
y
Standards
S
t
a
n
d
a
r
d
s
This
T
h
i
s
document
d
o
c
u
m
e
n
t
is
i
s
property
p
r
o
p
e
r
t
y
of
o
f
DRIMCO.
D
R
I
M
C
O
.
It
I
t
shall
s
h
a
l
l
neither
n
e
i
t
h
e
r
be
b
e
shown
s
h
o
w
n
to
t
o
Third
T
h
i
r
d
Parties
P
a
r
t
i
e
s
not
n
o
t
used
u
s
e
d
for
f
o
r
purposes
p
u
r
p
o
s
e
s
other
o
t
h
e
r
than
t
h
a
n
those
t
h
o
s
e
for
f
o
r
which
w
h
i
c
h
it
i
t
has
h
a
s
been
b
e
e
n
sent.
s
e
n
t
.
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0.00
0.00