Samir Abdon Campos Jabar
2026-03-17T08:31:13-03:00
2026-03-17T08:31:13-03:00
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TECHNICAL
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CLIENT:
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JOB:
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SPECIFICATION
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REDUC
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REFINARIA
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I-ET-5230.00-2221-500-APJ-001
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DESIGN
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WORD/V.2013/I-ET-5230.00-2221-500-APJ-001=A.doc
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INDEX
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REVISIONS
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FOR
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DATE
D
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11/11/2025
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EXECUTION
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TITLE:
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TECHNICAL
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SPECIFICATION
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I-ET-5230.00-2221-500-APJ-001
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t
i
o
n
s
mentioned
m
e
n
t
i
o
n
e
d
in
i
n
the
t
h
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Applicable
A
p
p
l
i
c
a
b
l
e
Standards
S
t
a
n
d
a
r
d
s
are
a
r
e
also
a
l
s
o
applicable.
a
p
p
l
i
c
a
b
l
e
.
3.1.3.
3
.
1
.
3
.
This
T
h
i
s
Technical
T
e
c
h
n
i
c
a
l
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
shall
s
h
a
l
l
take
t
a
k
e
precedence
p
r
e
c
e
d
e
n
c
e
over
o
v
e
r
the
t
h
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Applicable
A
p
p
l
i
c
a
b
l
e
Standards.
S
t
a
n
d
a
r
d
s
.
3.1.4.
3
.
1
.
4
.
Codes,
C
o
d
e
s
,
standards
s
t
a
n
d
a
r
d
s
and
a
n
d
technical
t
e
c
h
n
i
c
a
l
specifications
s
p
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c
i
f
i
c
a
t
i
o
n
s
listed
l
i
s
t
e
d
on
o
n
the
t
h
e
Contractual
C
o
n
t
r
a
c
t
u
a
l
Annex
A
n
n
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x
of
o
f
Applicable
A
p
p
l
i
c
a
b
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Standards
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t
a
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d
a
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d
s
and
a
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d
Documents
D
o
c
u
m
e
n
t
s
shall
s
h
a
l
l
also
a
l
s
o
be
b
e
used.
u
s
e
d
.
3.2.
3
.
2
.
PETROBRAS
P
E
T
R
O
B
R
A
S
Standards
S
t
a
n
d
a
r
d
s
N-253
N
-
2
5
3
-
-
Pressure
P
r
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s
s
u
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Vessel
V
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s
s
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l
Design
D
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s
i
g
n
N-266
N
-
2
6
6
-
-
Presentation
P
r
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s
e
n
t
a
t
i
o
n
of
o
f
Pressure
P
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s
s
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Vessel
V
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s
s
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l
Design
D
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s
i
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n
N-268
N
-
2
6
8
-
-
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F
a
b
r
i
c
a
t
i
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n
of
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f
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P
r
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s
s
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Vessel
V
e
s
s
e
l
N-269
N
-
2
6
9
-
-
Pressure
P
r
e
s
s
u
r
e
Vessel
V
e
s
s
e
l
Assembly
A
s
s
e
m
b
l
y
N-466
N
-
4
6
6
-
-
English
E
n
g
l
i
s
h
–
–
Design
D
e
s
i
g
n
of
o
f
Shell-and-Tube
S
h
e
l
l
-
a
n
d
-
T
u
b
e
Heat
H
e
a
t
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E
x
c
h
a
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g
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r
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1
4
9
2
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S
h
e
l
l
and
a
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d
Tube
T
u
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e
a
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E
x
c
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g
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r
–
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Data
D
a
t
a
Sheet
S
h
e
e
t
N-1500
N
-
1
5
0
0
-
-
English
E
n
g
l
i
s
h
–
–
Pressure
P
r
e
s
s
u
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e
Vessel
V
e
s
s
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l
Drawing
D
r
a
w
i
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g
and
a
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d
Data
D
a
t
a
Sheet
S
h
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t
Form
F
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m
N-1706
N
-
1
7
0
6
-
-
Additional
A
d
d
i
t
i
o
n
a
l
Requirements
R
e
q
u
i
r
e
m
e
n
t
s
for
f
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Pressure
P
r
e
s
s
u
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Vessel
V
e
s
s
e
l
Subject
S
u
b
j
e
c
t
to
t
o
Wet
W
e
t
H2S
H
2
S
Service
S
e
r
v
i
c
e
N-1707
N
-
1
7
0
7
-
-
Projeto
P
r
o
j
e
t
o
de
d
e
Vaso
V
a
s
o
de
d
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Pressão
P
r
e
s
s
ã
o
com
c
o
m
Revestimento
R
e
v
e
s
t
i
m
e
n
t
o
Metálico
M
e
t
á
l
i
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o
N-1710
N
-
1
7
1
0
-
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English
E
n
g
l
i
s
h
-
-
Coding
C
o
d
i
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g
of
o
f
Technical
T
e
c
h
n
i
c
a
l
Engineering
E
n
g
i
n
e
e
r
i
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g
Documents
D
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u
m
e
n
t
s
N-2054
N
-
2
0
5
4
-
-
English
E
n
g
l
i
s
h
-
-
Internal
I
n
t
e
r
n
a
l
and
a
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d
External
E
x
t
e
r
n
a
l
Accessories
A
c
c
e
s
s
o
r
i
e
s
for
f
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Pressure
P
r
e
s
s
u
r
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Vessels
V
e
s
s
e
l
s
N-2064
N
-
2
0
6
4
-
-
English
E
n
g
l
i
s
h
–
–
Issuance
I
s
s
u
a
n
c
e
and
a
n
d
Revision
R
e
v
i
s
i
o
n
of
o
f
Design
D
e
s
i
g
n
Documents
D
o
c
u
m
e
n
t
s
N-2941
N
-
2
9
4
1
-
-
Personal
P
e
r
s
o
n
a
l
Competencies
C
o
m
p
e
t
e
n
c
i
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s
for
f
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r
Inspection
I
n
s
p
e
c
t
i
o
n
Activities
A
c
t
i
v
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i
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s
N-0002
N
-
0
0
0
2
-
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Revestimento
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e
v
e
s
t
i
m
e
n
t
o
Anticorrosivo
A
n
t
i
c
o
r
r
o
s
i
v
o
de
d
e
Equipamento
E
q
u
i
p
a
m
e
n
t
o
Industrial
I
n
d
u
s
t
r
i
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TITLE:
T
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TECHNICAL
T
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C
H
N
I
C
A
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SPECIFICATION
S
P
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C
I
F
I
C
A
T
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N
N
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of
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/
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INTERNA
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N
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3.3.
3
.
3
.
PETROBRAS
P
E
T
R
O
B
R
A
S
Technical
T
e
c
h
n
i
c
a
l
Specifications
S
p
e
c
i
f
i
c
a
t
i
o
n
s
I-ET-0000.00-0000-500-PEI-001
I
-
E
T
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0
0
0
0
.
0
0
-
0
0
0
0
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0
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I
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0
0
1
(Compliance
(
C
o
m
p
l
i
a
n
c
e
with
w
i
t
h
NR-13
N
R
-
1
3
Requirements
R
e
q
u
i
r
e
m
e
n
t
s
for
f
o
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Pressure
P
r
e
s
s
u
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Vessels)
V
e
s
s
e
l
s
)
I-ET-0000.00-0000-500-PEI-003
I
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E
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-
0
0
0
0
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0
0
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0
0
0
0
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5
0
0
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P
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I
-
0
0
3
(Procedure
(
P
r
o
c
e
d
u
r
e
for
f
o
r
Performing
P
e
r
f
o
r
m
i
n
g
Stress
S
t
r
e
s
s
Analysis
A
n
a
l
y
s
i
s
by
b
y
Means
M
e
a
n
s
of
o
f
Finite
F
i
n
i
t
e
Element
E
l
e
m
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t
Method
M
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t
h
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d
(FEM)
(
F
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)
I-ET-0000.00-0000-500-PEI-004
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I
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0
0
4
(Rules
(
R
u
l
e
s
to
t
o
Calculate
C
a
l
c
u
l
a
t
e
Wind
W
i
n
d
Loading
L
o
a
d
i
n
g
on
o
n
Equipment)
E
q
u
i
p
m
e
n
t
)
I-ET-0000.00-0000-500-PEI-005
I
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0
0
0
0
.
0
0
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0
0
0
0
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5
0
0
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P
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I
-
0
0
5
(Maximum
(
M
a
x
i
m
u
m
Allowable
A
l
l
o
w
a
b
l
e
Loads
L
o
a
d
s
on
o
n
Pressure
P
r
e
s
s
u
r
e
Vessel
V
e
s
s
e
l
Nozzles)
N
o
z
z
l
e
s
)
3.4.
3
.
4
.
Brazilian
B
r
a
z
i
l
i
a
n
Regulation
R
e
g
u
l
a
t
i
o
n
and
a
n
d
Standards
S
t
a
n
d
a
r
d
s
Brazilian
B
r
a
z
i
l
i
a
n
Ministry
M
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n
i
s
t
r
y
of
o
f
Economy
E
c
o
n
o
m
y
Regulation
R
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g
u
l
a
t
i
o
n
no.
n
o
.
NR-13
N
R
-
1
3
(Norma
(
N
o
r
m
a
Regulamentadora
R
e
g
u
l
a
m
e
n
t
a
d
o
r
a
de
d
e
Caldeiras,
C
a
l
d
e
i
r
a
s
,
Vasos
V
a
s
o
s
de
d
e
Pressão
P
r
e
s
s
ã
o
e
e
Tubulações
T
u
b
u
l
a
ç
õ
e
s
e
e
Tanques
T
a
n
q
u
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s
Metálicos
M
e
t
á
l
i
c
o
s
de
d
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Armazenamento)
A
r
m
a
z
e
n
a
m
e
n
t
o
)
3.5.
3
.
5
.
References
R
e
f
e
r
e
n
c
e
s
Documents
D
o
c
u
m
e
n
t
s
DE-5230.00-2221-944-APJ-002
D
E
-
5
2
3
0
.
0
0
-
2
2
2
1
-
9
4
4
-
A
P
J
-
0
0
2
(Fluxograma
(
F
l
u
x
o
g
r
a
m
a
de
d
e
Engenharia
E
n
g
e
n
h
a
r
i
a
–
–
Separadores)
S
e
p
a
r
a
d
o
r
e
s
)
I-RM-5230.00-2221-321-APJ-002
I
-
R
M
-
5
2
3
0
.
0
0
-
2
2
2
1
-
3
2
1
-
A
P
J
-
0
0
2
(Material
(
M
a
t
e
r
i
a
l
Requisition
R
e
q
u
i
s
i
t
i
o
n
for
f
o
r
Wet
W
e
t
Gas
G
a
s
Compressor
C
o
m
p
r
e
s
s
o
r
Supply
S
u
p
p
l
y
C-504)
C
-
5
0
4
)
3.6.
3
.
6
.
Codes
C
o
d
e
s
NACE
N
A
C
E
Std
S
t
d
MR103
M
R
1
0
3
/
/
ISO
I
S
O
17495-1
1
7
4
9
5
-
1
(Petroleum,
(
P
e
t
r
o
l
e
u
m
,
petrochemical
p
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t
r
o
c
h
e
m
i
c
a
l
and
a
n
d
natural
n
a
t
u
r
a
l
gas
g
a
s
industries
i
n
d
u
s
t
r
i
e
s
-
-
Metallic
M
e
t
a
l
l
i
c
materials
m
a
t
e
r
i
a
l
s
resistant
r
e
s
i
s
t
a
n
t
to
t
o
sulfide
s
u
l
f
i
d
e
stress
s
t
r
e
s
s
cracking
c
r
a
c
k
i
n
g
in
i
n
corrosive
c
o
r
r
o
s
i
v
e
petroleum
p
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t
r
o
l
e
u
m
refining
r
e
f
i
n
i
n
g
environments)
e
n
v
i
r
o
n
m
e
n
t
s
)
NACE
N
A
C
E
Std
S
t
d
MR0175
M
R
0
1
7
5
/
/
ISO
I
S
O
15156-1
1
5
1
5
6
-
1
(Petroleum
(
P
e
t
r
o
l
e
u
m
and
a
n
d
natural
n
a
t
u
r
a
l
gas
g
a
s
industries—
i
n
d
u
s
t
r
i
e
s
—
Materials
M
a
t
e
r
i
a
l
s
for
f
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use
u
s
e
in
i
n
H2S-containing
H
2
S
-
c
o
n
t
a
i
n
i
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g
Environments
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v
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n
m
e
n
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s
in
i
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oil
o
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and
a
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gas
g
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production)
p
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i
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)
ASME
A
S
M
E
Seção
S
e
ç
ã
o
VIII,
V
I
I
I
,
Divisão
D
i
v
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s
ã
o
1
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and
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Vessel
V
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Code)
C
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ASME
A
S
M
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B16.5
B
1
6
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5
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P
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l
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and
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Fittings)
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)
ASTM
A
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Society
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(
S
t
a
n
d
a
r
d
s
Of
O
f
Tubular
T
u
b
u
l
a
r
Exchanger
E
x
c
h
a
n
g
e
r
Manufacturer
M
a
n
u
f
a
c
t
u
r
e
r
Association)
A
s
s
o
c
i
a
t
i
o
n
)
WRC
W
R
C
107/297
1
0
7
/
2
9
7
(Local
(
L
o
c
a
l
Stresses
S
t
r
e
s
s
e
s
in
i
n
Spherical
S
p
h
e
r
i
c
a
l
and
a
n
d
Cylindrical
C
y
l
i
n
d
r
i
c
a
l
Shells
S
h
e
l
l
s
Due
D
u
e
to
t
o
External
E
x
t
e
r
n
a
l
Loadings)
L
o
a
d
i
n
g
s
)
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
AREA:
A
R
E
A
:
TITLE:
T
I
T
L
E
:
-
DESIGN
D
E
S
I
G
N
CRITERIA
C
R
I
T
E
R
I
A
4.1.
4
.
1
.
General
G
e
n
e
r
a
l
TECHNICAL
T
E
C
H
N
I
C
A
L
SPECIFICATION
S
P
E
C
I
F
I
C
A
T
I
O
N
N
N
O
O
I-ET-5230.00-2221-500-APJ-001
I
-
E
T
-
5
2
3
0
.
0
0
-
2
2
2
1
-
5
0
0
-
A
P
J
-
0
0
1
U-1250
U
-
1
2
5
0
DESIGN
D
E
S
I
G
N
CRITERIA
C
R
I
T
E
R
I
A
–
–
STATIC
S
T
A
T
I
C
EQUIPMENT
E
Q
U
I
P
M
E
N
T
D-591
D
-
5
9
1
AND
A
N
D
E-590
E
-
5
9
0
SHEET:
S
H
E
E
T
:
REV.
R
E
V
.
5
5
of
o
f
9
9
SRGE/SI-IV/IES
S
R
G
E
/
S
I
-
I
V
/
I
E
S
INTERNA
I
N
T
E
R
N
A
4.1.1.
4
.
1
.
1
.
The
T
h
e
static
s
t
a
t
i
c
equipment
e
q
u
i
p
m
e
n
t
D-591
D
-
5
9
1
and
a
n
d
E-590
E
-
5
9
0
shall
s
h
a
l
l
be
b
e
designed
d
e
s
i
g
n
e
d
and
a
n
d
constructed
c
o
n
s
t
r
u
c
t
e
d
in
i
n
accordance
a
c
c
o
r
d
a
n
c
e
with
w
i
t
h
ASME-VIII
A
S
M
E
-
V
I
I
I
Div.
D
i
v
.
1,
1
,
supplied
s
u
p
p
l
i
e
d
with
w
i
t
h
the
t
h
e
ASME
A
S
M
E
U
U
Stamp.
S
t
a
m
p
.
4.1.2.
4
.
1
.
2
.
The
T
h
e
VENDOR
V
E
N
D
O
R
shall
s
h
a
l
l
be
b
e
responsible
r
e
s
p
o
n
s
i
b
l
e
for
f
o
r
performing
p
e
r
f
o
r
m
i
n
g
detailed
d
e
t
a
i
l
e
d
engineering
e
n
g
i
n
e
e
r
i
n
g
in
i
n
accordance
a
c
c
o
r
d
a
n
c
e
with
w
i
t
h
PETROBRAS
P
E
T
R
O
B
R
A
S
design
d
e
s
i
g
n
specifications
s
p
e
c
i
f
i
c
a
t
i
o
n
s
NI-253,
N
I
-
2
5
3
,
NI-466,
N
I
-
4
6
6
,
and
a
n
d
NI-1706,
N
I
-
1
7
0
6
,
which
w
h
i
c
h
shall
s
h
a
l
l
serve
s
e
r
v
e
as
a
s
the
t
h
e
basis
b
a
s
i
s
for
f
o
r
the
t
h
e
design,
d
e
s
i
g
n
,
fabrication,
f
a
b
r
i
c
a
t
i
o
n
,
and
a
n
d
testing
t
e
s
t
i
n
g
of
o
f
static
s
t
a
t
i
c
equipment
e
q
u
i
p
m
e
n
t
D-591
D
-
5
9
1
and
a
n
d
E-590.
E
-
5
9
0
.
4.1.3.
4
.
1
.
3
.
In
I
n
the
t
h
e
event
e
v
e
n
t
that
t
h
a
t
the
t
h
e
VENDOR
V
E
N
D
O
R
engages
e
n
g
a
g
e
s
subcontractor(s)
s
u
b
c
o
n
t
r
a
c
t
o
r
(
s
)
for
f
o
r
the
t
h
e
design,
d
e
s
i
g
n
,
fabrication,
f
a
b
r
i
c
a
t
i
o
n
,
and
a
n
d
testing
t
e
s
t
i
n
g
of
o
f
static
s
t
a
t
i
c
equipment,
e
q
u
i
p
m
e
n
t
,
the
t
h
e
VENDOR
V
E
N
D
O
R
shall
s
h
a
l
l
be
b
e
responsible
r
e
s
p
o
n
s
i
b
l
e
for
f
o
r
ensuring
e
n
s
u
r
i
n
g
that
t
h
a
t
such
s
u
c
h
subcontractors
s
u
b
c
o
n
t
r
a
c
t
o
r
s
comply
c
o
m
p
l
y
with
w
i
t
h
the
t
h
e
technical
t
e
c
h
n
i
c
a
l
requirements
r
e
q
u
i
r
e
m
e
n
t
s
of
o
f
PETROBRAS
P
E
T
R
O
B
R
A
S
standards
s
t
a
n
d
a
r
d
s
NI-253,
N
I
-
2
5
3
,
NI-466,
N
I
-
4
6
6
,
and
a
n
d
NI-1706.
N
I
-
1
7
0
6
.
4.1.4.
4
.
1
.
4
.
Minimum
M
i
n
i
m
u
m
conditions
c
o
n
d
i
t
i
o
n
s
required
r
e
q
u
i
r
e
d
for
f
o
r
E-590
E
-
5
9
0
Heat
H
e
a
t
Exchanger
E
x
c
h
a
n
g
e
r
-
-
Water
W
a
t
e
r
cooled
c
o
o
l
e
d
heat
h
e
a
t
exchangers
e
x
c
h
a
n
g
e
r
s
shall
s
h
a
l
l
have
h
a
v
e
the
t
h
e
water
w
a
t
e
r
located
l
o
c
a
t
e
d
into
i
n
t
o
the
t
h
e
tubes.
t
u
b
e
s
.
-
-
Cooling
C
o
o
l
i
n
g
water
w
a
t
e
r
deposit
d
e
p
o
s
i
t
coefficient
c
o
e
f
f
i
c
i
e
n
t
is
i
s
0.0004
0
.
0
0
0
4
m².°C.h/kcal.
m
²
.
°
C
.
h
/
k
c
a
l
.
-
-
Minimum
M
i
n
i
m
u
m
cooling
c
o
o
l
i
n
g
water
w
a
t
e
r
velocity
v
e
l
o
c
i
t
y
on
o
n
tube
t
u
b
e
side
s
i
d
e
is
i
s
1.0
1
.
0
m/s.
m
/
s
.
-
-
The
T
h
e
use
u
s
e
of
o
f
U-tubes
U
-
t
u
b
e
s
for
f
o
r
cooling
c
o
o
l
i
n
g
water
w
a
t
e
r
is
i
s
not
n
o
t
allowed.
a
l
l
o
w
e
d
.
4.1.5.
4
.
1
.
5
.
Minimum
M
i
n
i
m
u
m
Material
M
a
t
e
r
i
a
l
specification
s
p
e
c
i
f
i
c
a
t
i
o
n
for
f
o
r
Heat
H
e
a
t
Exchanger,
E
x
c
h
a
n
g
e
r
,
Pressure
P
r
e
s
s
u
r
e
Vessel
V
e
s
s
e
l
and
a
n
d
Internals
I
n
t
e
r
n
a
l
s
4.1.5.1
4
.
1
.
5
.
1
Vessel
V
e
s
s
e
l
D-591
D
-
5
9
1
Special
S
p
e
c
i
a
l
Service
S
e
r
v
i
c
e
Wet
W
e
t
H2S
H
2
S
–
–
NI-1706
N
I
-
1
7
0
6
Category
C
a
t
e
g
o
r
y
1
1
Corrosion
C
o
r
r
o
s
i
o
n
Allowance
A
l
l
o
w
a
n
c
e
6mm
6
m
m
PWHT
P
W
H
T
Yes
Y
e
s
(Wet
(
W
e
t
H2S
H
2
S
Service)
S
e
r
v
i
c
e
)
MATERIALS
M
A
T
E
R
I
A
L
S
Shell
S
h
e
l
l
Carbon
C
a
r
b
o
n
Steel
S
t
e
e
l
SA-516
S
A
-
5
1
6
Gr.
G
r
.
60
6
0
Nozzle
N
o
z
z
l
e
Necks
N
e
c
k
s
Carbon
C
a
r
b
o
n
Steel
S
t
e
e
l
SA-106
S
A
-
1
0
6
Gr.
G
r
.
B
B
Nozzles
N
o
z
z
l
e
s
Carbon
C
a
r
b
o
n
Steel
S
t
e
e
l
SA-105
S
A
-
1
0
5
/
/
SA-106
S
A
-
1
0
6
Gr.
G
r
.
B/
B
/
SA-516
S
A
-
5
1
6
Gr.
G
r
.
60
6
0
Internals
I
n
t
e
r
n
a
l
s
(removable
(
r
e
m
o
v
a
b
l
e
and
a
n
d
welded)
w
e
l
d
e
d
)
Carbon
C
a
r
b
o
n
Steel
S
t
e
e
l
SA-516
S
A
-
5
1
6
Gr.
G
r
.
60
6
0
Demister
D
e
m
i
s
t
e
r
Stainless
S
t
a
i
n
l
e
s
s
Steel
S
t
e
e
l
304/304L
3
0
4
/
3
0
4
L
Special
S
p
e
c
i
a
l
Service:
S
e
r
v
i
c
e
:
Wet
W
e
t
H2S
H
2
S
-
-
For
F
o
r
base
b
a
s
e
material,
m
a
t
e
r
i
a
l
,
design
d
e
s
i
g
n
and
a
n
d
fabrication
f
a
b
r
i
c
a
t
i
o
n
additional
a
d
d
i
t
i
o
n
a
l
requirements,
r
e
q
u
i
r
e
m
e
n
t
s
,
see
s
e
e
PETROBRAS
P
E
T
R
O
B
R
A
S
NI-1706
N
I
-
1
7
0
6
-
-
Category
C
a
t
e
g
o
r
y
1.
1
.
4.1.5.2
4
.
1
.
5
.
2
Heat
H
e
a
t
Exchanger
E
x
c
h
a
n
g
e
r
E-590
E
-
5
9
0
Shell
S
h
e
l
l
side
s
i
d
e
Tube
T
u
b
e
side
s
i
d
e
Special
S
p
e
c
i
a
l
Service
S
e
r
v
i
c
e
Wet
W
e
t
H2S
H
2
S
–
–
NI-1706
N
I
-
1
7
0
6
Category
C
a
t
e
g
o
r
y
1
1
-
-
Corrosion
C
o
r
r
o
s
i
o
n
Allowance
A
l
l
o
w
a
n
c
e
6mm
6
m
m
3mm
3
m
m
PWHT
P
W
H
T
Yes
Y
e
s
(Wet
(
W
e
t
H2S
H
2
S
Service)
S
e
r
v
i
c
e
)
-
-
MATERIALS
M
A
T
E
R
I
A
L
S
Shell
S
h
e
l
l
Carbon
C
a
r
b
o
n
Steel
S
t
e
e
l
SA-516
S
A
-
5
1
6
+
+
6mm
6
m
m
c.a.
c
.
a
.
Tubes
T
u
b
e
s
Duplex
D
u
p
l
e
x
Stainless
S
t
a
i
n
l
e
s
s
Steel
S
t
e
e
l
SA-789
S
A
-
7
8
9
UNS
U
N
S
S31803
S
3
1
8
0
3
(seamless)
(
s
e
a
m
l
e
s
s
)
Channel
C
h
a
n
n
e
l
Carbon
C
a
r
b
o
n
Steel
S
t
e
e
l
SA-516
S
A
-
5
1
6
+
+
3mm
3
m
m
c.a.
c
.
a
.
Tubesheet
T
u
b
e
s
h
e
e
t
Carbon
C
a
r
b
o
n
Steel
S
t
e
e
l
SA-516
S
A
-
5
1
6
+
+
6mm
6
m
m
c.a.
c
.
a
.
shell
s
h
e
l
l
side
s
i
d
e
+
+
3mm
3
m
m
clad
c
l
a
d
SS304L
S
S
3
0
4
L
tube
t
u
b
e
side
s
i
d
e
Baffles
B
a
f
f
l
e
s
Stainless
S
t
a
i
n
l
e
s
s
Steel
S
t
e
e
l
304/304L
3
0
4
/
3
0
4
L
Special
S
p
e
c
i
a
l
Service:
S
e
r
v
i
c
e
:
Wet
W
e
t
H2S
H
2
S
-
-
For
F
o
r
base
b
a
s
e
material,
m
a
t
e
r
i
a
l
,
design
d
e
s
i
g
n
and
a
n
d
fabrication
f
a
b
r
i
c
a
t
i
o
n
additional
a
d
d
i
t
i
o
n
a
l
requirements,
r
e
q
u
i
r
e
m
e
n
t
s
,
see
s
e
e
PETROBRAS
P
E
T
R
O
B
R
A
S
NI-1706
N
I
-
1
7
0
6
-
-
Category
C
a
t
e
g
o
r
y
1.
1
.
A
A
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
AREA:
A
R
E
A
:
TITLE:
T
I
T
L
E
:
TECHNICAL
T
E
C
H
N
I
C
A
L
SPECIFICATION
S
P
E
C
I
F
I
C
A
T
I
O
N
N
N
O
O
I-ET-5230.00-2221-500-APJ-001
I
-
E
T
-
5
2
3
0
.
0
0
-
2
2
2
1
-
5
0
0
-
A
P
J
-
0
0
1
U-1250
U
-
1
2
5
0
DESIGN
D
E
S
I
G
N
CRITERIA
C
R
I
T
E
R
I
A
–
–
STATIC
S
T
A
T
I
C
EQUIPMENT
E
Q
U
I
P
M
E
N
T
D-591
D
-
5
9
1
AND
A
N
D
E-590
E
-
5
9
0
SHEET:
S
H
E
E
T
:
REV.
R
E
V
.
6
6
of
o
f
9
9
SRGE/SI-IV/IES
S
R
G
E
/
S
I
-
I
V
/
I
E
S
INTERNA
I
N
T
E
R
N
A
4.1.6.
4
.
1
.
6
.
The
T
h
e
equipment
e
q
u
i
p
m
e
n
t
lifting
l
i
f
t
i
n
g
devices
d
e
v
i
c
e
s
as
a
s
tailing
t
a
i
l
i
n
g
lugs,
l
u
g
s
,
trunnions
t
r
u
n
n
i
o
n
s
and
a
n
d
lifting
l
i
f
t
i
n
g
lugs,
l
u
g
s
,
including
i
n
c
l
u
d
i
n
g
welds,
w
e
l
d
s
,
shall
s
h
a
l
l
be
b
e
designed
d
e
s
i
g
n
e
d
to
t
o
withstand
w
i
t
h
s
t
a
n
d
the
t
h
e
equipment
e
q
u
i
p
m
e
n
t
weight
w
e
i
g
h
t
considering
c
o
n
s
i
d
e
r
i
n
g
a
a
minimum
m
i
n
i
m
u
m
impact
i
m
p
a
c
t
factor
f
a
c
t
o
r
multiplier
m
u
l
t
i
p
l
i
e
r
of
o
f
1.5
1
.
5
and
a
n
d
the
t
h
e
allowable
a
l
l
o
w
a
b
l
e
stress
s
t
r
e
s
s
used
u
s
e
d
in
i
n
the
t
h
e
design
d
e
s
i
g
n
calculations
c
a
l
c
u
l
a
t
i
o
n
s
of
o
f
lifting
l
i
f
t
i
n
g
devices
d
e
v
i
c
e
s
shall
s
h
a
l
l
be
b
e
67%
6
7
%
of
o
f
the
t
h
e
material
m
a
t
e
r
i
a
l
yield
y
i
e
l
d
stress,
s
t
r
e
s
s
,
unless
u
n
l
e
s
s
otherwise
o
t
h
e
r
w
i
s
e
specified
s
p
e
c
i
f
i
e
d
on
o
n
mechanical
m
e
c
h
a
n
i
c
a
l
drawing.
d
r
a
w
i
n
g
.
The
T
h
e
design
d
e
s
i
g
n
shall
s
h
a
l
l
be
b
e
performed
p
e
r
f
o
r
m
e
d
considering
c
o
n
s
i
d
e
r
i
n
g
the
t
h
e
equipment
e
q
u
i
p
m
e
n
t
in
i
n
horizontal
h
o
r
i
z
o
n
t
a
l
and
a
n
d
vertical
v
e
r
t
i
c
a
l
position.
p
o
s
i
t
i
o
n
.
The
T
h
e
lifting
l
i
f
t
i
n
g
weight
w
e
i
g
h
t
shall
s
h
a
l
l
be
b
e
defined
d
e
f
i
n
e
d
as
a
s
shop
s
h
o
p
weight
w
e
i
g
h
t
plus
p
l
u
s
insulation,
i
n
s
u
l
a
t
i
o
n
,
ladders,
l
a
d
d
e
r
s
,
platforms,
p
l
a
t
f
o
r
m
s
,
main
m
a
i
n
pipelines
p
i
p
e
l
i
n
e
s
and
a
n
d
fireproofing.
f
i
r
e
p
r
o
o
f
i
n
g
.
The
T
h
e
internal
i
n
t
e
r
n
a
l
packing
p
a
c
k
i
n
g
or
o
r
trays
t
r
a
y
s
shall
s
h
a
l
l
be
b
e
excluded
e
x
c
l
u
d
e
d
in
i
n
lifting
l
i
f
t
i
n
g
weight.
w
e
i
g
h
t
.
4.1.7.
4
.
1
.
7
.
In
I
n
addition
a
d
d
i
t
i
o
n
to
t
o
the
t
h
e
requirements
r
e
q
u
i
r
e
m
e
n
t
s
indicated
i
n
d
i
c
a
t
e
d
in
i
n
the
t
h
e
applicable
a
p
p
l
i
c
a
b
l
e
PETROBRAS
P
E
T
R
O
B
R
A
S
Standards,
S
t
a
n
d
a
r
d
s
,
the
t
h
e
items
i
t
e
m
s
presented
p
r
e
s
e
n
t
e
d
below
b
e
l
o
w
shall
s
h
a
l
l
be
b
e
observed.
o
b
s
e
r
v
e
d
.
4.2.
4
.
2
.
Pressure
P
r
e
s
s
u
r
e
Vessels
V
e
s
s
e
l
s
4.2.1.
4
.
2
.
1
.
Facilities
F
a
c
i
l
i
t
i
e
s
shall
s
h
a
l
l
be
b
e
provided
p
r
o
v
i
d
e
d
for
f
o
r
the
t
h
e
removal
r
e
m
o
v
a
l
of
o
f
the
t
h
e
packing,
p
a
c
k
i
n
g
,
catalyst
c
a
t
a
l
y
s
t
and
a
n
d
appurtenances
a
p
p
u
r
t
e
n
a
n
c
e
s
(manholes,
(
m
a
n
h
o
l
e
s
,
platforms,
p
l
a
t
f
o
r
m
s
,
etc.)
e
t
c
.
)
for
f
o
r
maintenance
m
a
i
n
t
e
n
a
n
c
e
purpose.
p
u
r
p
o
s
e
.
4.2.2.
4
.
2
.
2
.
For
F
o
r
all
a
l
l
equipment
e
q
u
i
p
m
e
n
t
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
the
t
h
e
ASME
A
S
M
E
Code,
C
o
d
e
,
Section
S
e
c
t
i
o
n
VIII,
V
I
I
I
,
Division
D
i
v
i
s
i
o
n
1
1
or
o
r
2,
2
,
the
t
h
e
designer
d
e
s
i
g
n
e
r
shall
s
h
a
l
l
demonstrate,
d
e
m
o
n
s
t
r
a
t
e
,
in
i
n
the
t
h
e
calculation
c
a
l
c
u
l
a
t
i
o
n
sheets,
s
h
e
e
t
s
,
the
t
h
e
evaluation
e
v
a
l
u
a
t
i
o
n
for
f
o
r
impact
i
m
p
a
c
t
test
t
e
s
t
requirements
r
e
q
u
i
r
e
m
e
n
t
s
of
o
f
each
e
a
c
h
vessel
v
e
s
s
e
l
component
c
o
m
p
o
n
e
n
t
based
b
a
s
e
d
on
o
n
its
i
t
s
individual
i
n
d
i
v
i
d
u
a
l
material
m
a
t
e
r
i
a
l
classification,
c
l
a
s
s
i
f
i
c
a
t
i
o
n
,
thickness
t
h
i
c
k
n
e
s
s
and
a
n
d
the
t
h
e
rated
r
a
t
e
d
minimum
m
i
n
i
m
u
m
design
d
e
s
i
g
n
metal
m
e
t
a
l
temperature
t
e
m
p
e
r
a
t
u
r
e
(MDMT).
(
M
D
M
T
)
.
4.2.3.
4
.
2
.
3
.
For
F
o
r
horizontal
h
o
r
i
z
o
n
t
a
l
vessels
v
e
s
s
e
l
s
with
w
i
t
h
slope,
s
l
o
p
e
,
the
t
h
e
nozzle
n
o
z
z
l
e
location
l
o
c
a
t
i
o
n
shall
s
h
a
l
l
comply
c
o
m
p
l
y
with
w
i
t
h
the
t
h
e
sketch
s
k
e
t
c
h
showed
s
h
o
w
e
d
as
a
s
FIGURE
F
I
G
U
R
E
1.
1
.
Despites
D
e
s
p
i
t
e
s
the
t
h
e
slope,
s
l
o
p
e
,
all
a
l
l
nozzles
n
o
z
z
l
e
s
shall
s
h
a
l
l
be
b
e
in
i
n
vertical
v
e
r
t
i
c
a
l
position.
p
o
s
i
t
i
o
n
.
4.2.4.
4
.
2
.
4
.
For
F
o
r
horizontal
h
o
r
i
z
o
n
t
a
l
vessels
v
e
s
s
e
l
s
and
a
n
d
heat
h
e
a
t
exchangers,
e
x
c
h
a
n
g
e
r
s
,
with
w
i
t
h
operating
o
p
e
r
a
t
i
n
g
weight
w
e
i
g
h
t
exceeding
e
x
c
e
e
d
i
n
g
20
2
0
tons,
t
o
n
s
,
PTFE
P
T
F
E
(Polytetrafluoroethylene)
(
P
o
l
y
t
e
t
r
a
f
l
u
o
r
o
e
t
h
y
l
e
n
e
)
plates
p
l
a
t
e
s
shall
s
h
a
l
l
be
b
e
provided
p
r
o
v
i
d
e
d
in
i
n
the
t
h
e
sliding
s
l
i
d
i
n
g
saddle.
s
a
d
d
l
e
.
The
T
h
e
compression
c
o
m
p
r
e
s
s
i
o
n
strength
s
t
r
e
n
g
t
h
and
a
n
d
deformation
d
e
f
o
r
m
a
t
i
o
n
of
o
f
PTFE
P
T
F
E
(Polytetrafluoroethylene)
(
P
o
l
y
t
e
t
r
a
f
l
u
o
r
o
e
t
h
y
l
e
n
e
)
plates,
p
l
a
t
e
s
,
due
d
u
e
to
t
o
compression
c
o
m
p
r
e
s
s
i
o
n
load
l
o
a
d
on
o
n
the
t
h
e
slide
s
l
i
d
e
saddle,
s
a
d
d
l
e
,
shall
s
h
a
l
l
be
b
e
evaluated
e
v
a
l
u
a
t
e
d
in
i
n
order
o
r
d
e
r
to
t
o
avoid
a
v
o
i
d
contact
c
o
n
t
a
c
t
between
b
e
t
w
e
e
n
metallic
m
e
t
a
l
l
i
c
plates.
p
l
a
t
e
s
.
4.2.5.
4
.
2
.
5
.
Vortex
V
o
r
t
e
x
breakers
b
r
e
a
k
e
r
s
shall
s
h
a
l
l
be
b
e
removable
r
e
m
o
v
a
b
l
e
(not
(
n
o
t
welded
w
e
l
d
e
d
to
t
o
the
t
h
e
equipment
e
q
u
i
p
m
e
n
t
shell),
s
h
e
l
l
)
,
in
i
n
order
o
r
d
e
r
to
t
o
make
m
a
k
e
easy
e
a
s
y
inspection
i
n
s
p
e
c
t
i
o
n
and
a
n
d
cleaning.
c
l
e
a
n
i
n
g
.
4.2.6.
4
.
2
.
6
.
The
T
h
e
circumferential
c
i
r
c
u
m
f
e
r
e
n
t
i
a
l
weld
w
e
l
d
of
o
f
Ring-Type
R
i
n
g
-
T
y
p
e
Flanges
F
l
a
n
g
e
s
designed
d
e
s
i
g
n
e
d
and
a
n
d
fabricated
f
a
b
r
i
c
a
t
e
d
according
a
c
c
o
r
d
i
n
g
to
t
o
Appendix
A
p
p
e
n
d
i
x
2,
2
,
Figure
F
i
g
u
r
e
(11)
(
1
1
)
of
o
f
ASME
A
S
M
E
BPVC
B
P
V
C
Section
S
e
c
t
i
o
n
VIII
V
I
I
I
Division
D
i
v
i
s
i
o
n
1
1
shall
s
h
a
l
l
be
b
e
UT
U
T
examined.
e
x
a
m
i
n
e
d
.
4.2.7.
4
.
2
.
7
.
The
T
h
e
stresses
s
t
r
e
s
s
e
s
analysis
a
n
a
l
y
s
i
s
of
o
f
nozzles
n
o
z
z
l
e
s
junctions
j
u
n
c
t
i
o
n
s
on
o
n
the
t
h
e
shell
s
h
e
l
l
and
a
n
d
heads
h
e
a
d
s
due
d
u
e
to
t
o
external
e
x
t
e
r
n
a
l
piping
p
i
p
i
n
g
loads
l
o
a
d
s
is
i
s
equipment
e
q
u
i
p
m
e
n
t
manufacturer’s
m
a
n
u
f
a
c
t
u
r
e
r
’
s
responsibility.
r
e
s
p
o
n
s
i
b
i
l
i
t
y
.
4.3.
4
.
3
.
Heat
H
e
a
t
Exchangers
E
x
c
h
a
n
g
e
r
s
4.3.1.
4
.
3
.
1
.
TEMA
T
E
M
A
Class
C
l
a
s
s
R
R
-
-
Type
T
y
p
e
AJS.
A
J
S
.
4.3.2.
4
.
3
.
2
.
Tube
T
u
b
e
bundles
b
u
n
d
l
e
s
shall
s
h
a
l
l
be
b
e
identified
i
d
e
n
t
i
f
i
e
d
in
i
n
the
t
h
e
back
b
a
c
k
area
a
r
e
a
of
o
f
fixed
f
i
x
e
d
tube-sheet,
t
u
b
e
-
s
h
e
e
t
,
by
b
y
three
t
h
r
e
e
mark
m
a
r
k
spaced
s
p
a
c
e
d
120
1
2
0
degrees
d
e
g
r
e
e
s
apart.
a
p
a
r
t
.
The
T
h
e
marks
m
a
r
k
s
shall
s
h
a
l
l
be
b
e
done
d
o
n
e
with
w
i
t
h
a
a
½”
½
”
steel
s
t
e
e
l
punch.
p
u
n
c
h
.
-
Heat
H
e
a
t
exchangers
e
x
c
h
a
n
g
e
r
s
with
w
i
t
h
one
o
n
e
tube
t
u
b
e
bundle:
b
u
n
d
l
e
:
FP-2001-1
F
P
-
2
0
0
1
-
1
-
-
tube
t
u
b
e
bundle
b
u
n
d
l
e
of
o
f
P-2001
P
-
2
0
0
1
FP-2001-2
F
P
-
2
0
0
1
-
2
-
-
spare
s
p
a
r
e
tube
t
u
b
e
bundle
b
u
n
d
l
e
of
o
f
P-2001
P
-
2
0
0
1
-
Heat
H
e
a
t
exchangers
e
x
c
h
a
n
g
e
r
s
with
w
i
t
h
interchangeable
i
n
t
e
r
c
h
a
n
g
e
a
b
l
e
tube
t
u
b
e
bundles:
b
u
n
d
l
e
s
:
FP-2002-1
F
P
-
2
0
0
2
-
1
and
a
n
d
FP-2002-2
F
P
-
2
0
0
2
-
2
-
-
interchangeable
i
n
t
e
r
c
h
a
n
g
e
a
b
l
e
tube
t
u
b
e
bundles
b
u
n
d
l
e
s
of
o
f
P-2002
P
-
2
0
0
2
A/B
A
/
B
FP-2002-3
F
P
-
2
0
0
2
-
3
-
-
spare
s
p
a
r
e
tube
t
u
b
e
bundles
b
u
n
d
l
e
s
of
o
f
P-2002
P
-
2
0
0
2
A/B
A
/
B
A
A
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
AREA:
A
R
E
A
:
TITLE:
T
I
T
L
E
:
TECHNICAL
T
E
C
H
N
I
C
A
L
SPECIFICATION
S
P
E
C
I
F
I
C
A
T
I
O
N
N
N
O
O
I-ET-5230.00-2221-500-APJ-001
I
-
E
T
-
5
2
3
0
.
0
0
-
2
2
2
1
-
5
0
0
-
A
P
J
-
0
0
1
U-1250
U
-
1
2
5
0
DESIGN
D
E
S
I
G
N
CRITERIA
C
R
I
T
E
R
I
A
–
–
STATIC
S
T
A
T
I
C
EQUIPMENT
E
Q
U
I
P
M
E
N
T
D-591
D
-
5
9
1
AND
A
N
D
E-590
E
-
5
9
0
-
Heat
H
e
a
t
exchangers
e
x
c
h
a
n
g
e
r
s
with
w
i
t
h
interchangeable
i
n
t
e
r
c
h
a
n
g
e
a
b
l
e
two
t
w
o
at
a
t
two
t
w
o
tube
t
u
b
e
bundles:
b
u
n
d
l
e
s
:
SHEET:
S
H
E
E
T
:
REV.
R
E
V
.
7
7
of
o
f
9
9
SRGE/SI-IV/IES
S
R
G
E
/
S
I
-
I
V
/
I
E
S
INTERNA
I
N
T
E
R
N
A
FP-2003
F
P
-
2
0
0
3
A/B-1
A
/
B
-
1
and
a
n
d
FP-2003
F
P
-
2
0
0
3
A/B-2
A
/
B
-
2
-
-
interchangeable
i
n
t
e
r
c
h
a
n
g
e
a
b
l
e
tube
t
u
b
e
bundles
b
u
n
d
l
e
s
of
o
f
P-2003
P
-
2
0
0
3
A/B
A
/
B
FP-2003
F
P
-
2
0
0
3
A/B-3
A
/
B
-
3
-
-
spare
s
p
a
r
e
tube
t
u
b
e
bundle
b
u
n
d
l
e
of
o
f
P-2003
P
-
2
0
0
3
A/B
A
/
B
FP-2003
F
P
-
2
0
0
3
C/D-1
C
/
D
-
1
and
a
n
d
FP-2003
F
P
-
2
0
0
3
C/D-2
C
/
D
-
2
-
-
interchangeable
i
n
t
e
r
c
h
a
n
g
e
a
b
l
e
tube
t
u
b
e
bundles
b
u
n
d
l
e
s
of
o
f
P-2003
P
-
2
0
0
3
C/D
C
/
D
FP-2003
F
P
-
2
0
0
3
C/D-3
C
/
D
-
3
-
-
spare
s
p
a
r
e
tube
t
u
b
e
bundle
b
u
n
d
l
e
of
o
f
P-2003
P
-
2
0
0
3
C/D
C
/
D
The
T
h
e
respective
r
e
s
p
e
c
t
i
v
e
equipment
e
q
u
i
p
m
e
n
t
tags
t
a
g
s
shall
s
h
a
l
l
also
a
l
s
o
identify
i
d
e
n
t
i
f
y
all
a
l
l
parts
p
a
r
t
s
of
o
f
heat
h
e
a
t
exchangers.
e
x
c
h
a
n
g
e
r
s
.
4.3.3.
4
.
3
.
3
.
The
T
h
e
following
f
o
l
l
o
w
i
n
g
heat
h
e
a
t
exchanger
e
x
c
h
a
n
g
e
r
components
c
o
m
p
o
n
e
n
t
s
shall
s
h
a
l
l
be
b
e
marked
m
a
r
k
e
d
with
w
i
t
h
a
a
1/2”
1
/
2
”
steel
s
t
e
e
l
punch:
p
u
n
c
h
:
-
Channel
C
h
a
n
n
e
l
cover;
c
o
v
e
r
;
-
Channel;
C
h
a
n
n
e
l
;
-
Floating
F
l
o
a
t
i
n
g
head
h
e
a
d
cover;
c
o
v
e
r
;
-
Bonnet;
B
o
n
n
e
t
;
-
Floating
F
l
o
a
t
i
n
g
head
h
e
a
d
backing-device
b
a
c
k
i
n
g
-
d
e
v
i
c
e
and
a
n
d
splice
s
p
l
i
c
e
plates;
p
l
a
t
e
s
;
-
Test
T
e
s
t
ring
r
i
n
g
and
a
n
d
test
t
e
s
t
flange.
f
l
a
n
g
e
.
4.3.4.
4
.
3
.
4
.
The
T
h
e
installation
i
n
s
t
a
l
l
a
t
i
o
n
of
o
f
nameplates
n
a
m
e
p
l
a
t
e
s
on
o
n
covers
c
o
v
e
r
s
channels
c
h
a
n
n
e
l
s
or
o
r
any
a
n
y
other
o
t
h
e
r
removable
r
e
m
o
v
a
b
l
e
parts
p
a
r
t
s
shall
s
h
a
l
l
be
b
e
avoided.
a
v
o
i
d
e
d
.
Preference
P
r
e
f
e
r
e
n
c
e
shall
s
h
a
l
l
be
b
e
given
g
i
v
e
n
to
t
o
a
a
visible
v
i
s
i
b
l
e
place
p
l
a
c
e
on
o
n
the
t
h
e
shell.
s
h
e
l
l
.
4.3.5.
4
.
3
.
5
.
All
A
l
l
heat
h
e
a
t
exchangers
e
x
c
h
a
n
g
e
r
s
shall
s
h
a
l
l
be
b
e
supplied
s
u
p
p
l
i
e
d
with
w
i
t
h
a
a
test
t
e
s
t
ring
r
i
n
g
and/or
a
n
d
/
o
r
a
a
test
t
e
s
t
flange.
f
l
a
n
g
e
.
For
F
o
r
those
t
h
o
s
e
operating
o
p
e
r
a
t
i
n
g
in
i
n
parallel
p
a
r
a
l
l
e
l
(interchangeable
(
i
n
t
e
r
c
h
a
n
g
e
a
b
l
e
units),
u
n
i
t
s
)
,
a
a
number
n
u
m
b
e
r
of
o
f
one
o
n
e
test
t
e
s
t
ring
r
i
n
g
/flange
/
f
l
a
n
g
e
shall
s
h
a
l
l
be
b
e
supplied
s
u
p
p
l
i
e
d
for
f
o
r
each
e
a
c
h
set
s
e
t
with
w
i
t
h
less
l
e
s
s
than
t
h
a
n
4
4
(four)
(
f
o
u
r
)
heat
h
e
a
t
exchanges,
e
x
c
h
a
n
g
e
s
,
and
a
n
d
for
f
o
r
greater
g
r
e
a
t
e
r
set,
s
e
t
,
two
t
w
o
test
t
e
s
t
rings
r
i
n
g
s
for
f
o
r
each
e
a
c
h
set
s
e
t
with
w
i
t
h
4
4
(four)
(
f
o
u
r
)
heat
h
e
a
t
exchanges.
e
x
c
h
a
n
g
e
s
.
4.3.6.
4
.
3
.
6
.
Two
T
w
o
spare
s
p
a
r
e
sets
s
e
t
s
of
o
f
gaskets
g
a
s
k
e
t
s
and
a
n
d
10%
1
0
%
of
o
f
the
t
h
e
bolts
b
o
l
t
s
of
o
f
the
t
h
e
heat
h
e
a
t
exchangers
e
x
c
h
a
n
g
e
r
s
main
m
a
i
n
flanges
f
l
a
n
g
e
s
shall
s
h
a
l
l
be
b
e
supplied.
s
u
p
p
l
i
e
d
.
4.3.7.
4
.
3
.
7
.
The
T
h
e
floating
f
l
o
a
t
i
n
g
head
h
e
a
d
configuration
c
o
n
f
i
g
u
r
a
t
i
o
n
shall
s
h
a
l
l
be
b
e
in
i
n
accordance
a
c
c
o
r
d
a
n
c
e
with
w
i
t
h
TEMA
T
E
M
A
item
i
t
e
m
RCB-5.
R
C
B
-
5
.
The
T
h
e
length
l
e
n
g
t
h
projections
p
r
o
j
e
c
t
i
o
n
s
indicated
i
n
d
i
c
a
t
e
d
on
o
n
Figure
F
i
g
u
r
e
RCB-5.141
R
C
B
-
5
.
1
4
1
of
o
f
TEMA
T
E
M
A
as
a
s
“OPTIONAL”
“
O
P
T
I
O
N
A
L
”
shall
s
h
a
l
l
be
b
e
mandatory.
m
a
n
d
a
t
o
r
y
.
The
T
h
e
STYLE
S
T
Y
L
E
“D”
“
D
”
configuration
c
o
n
f
i
g
u
r
a
t
i
o
n
on
o
n
Figure
F
i
g
u
r
e
RCB-5.141
R
C
B
-
5
.
1
4
1
of
o
f
TEMA
T
E
M
A
is
i
s
not
n
o
t
permitted.
p
e
r
m
i
t
t
e
d
.
4.3.8.
4
.
3
.
8
.
When
W
h
e
n
two
t
w
o
gaskets
g
a
s
k
e
t
s
are
a
r
e
compressed
c
o
m
p
r
e
s
s
e
d
by
b
y
the
t
h
e
same
s
a
m
e
bolting,
b
o
l
t
i
n
g
,
as
a
s
in
i
n
the
t
h
e
design
d
e
s
i
g
n
of
o
f
flange
f
l
a
n
g
e
pairs
p
a
i
r
s
used
u
s
e
d
to
t
o
contain
c
o
n
t
a
i
n
a
a
tubesheet,
t
u
b
e
s
h
e
e
t
,
for
f
o
r
both
b
o
t
h
side,
s
i
d
e
,
shall
s
h
a
l
l
be
b
e
used
u
s
e
d
the
t
h
e
same
s
a
m
e
gasket
g
a
s
k
e
t
material,
m
a
t
e
r
i
a
l
,
suitable
s
u
i
t
a
b
l
e
for
f
o
r
the
t
h
e
more
m
o
r
e
critical
c
r
i
t
i
c
a
l
condition
c
o
n
d
i
t
i
o
n
(see
(
s
e
e
also
a
l
s
o
TEMA
T
E
M
A
paragraph
p
a
r
a
g
r
a
p
h
R-6.2/CB-6.2
R
-
6
.
2
/
C
B
-
6
.
2
and
a
n
d
ASME
A
S
M
E
BPVC
B
P
V
C
Section
S
e
c
t
i
o
n
VIII
V
I
I
I
–
–
item
i
t
e
m
2.5.(a)
2
.
5
.
(
a
)
(2),
(
2
)
,
for
f
o
r
Division
D
i
v
i
s
i
o
n
1
1
and
a
n
d
item
i
t
e
m
4.16.2.4,
4
.
1
6
.
2
.
4
,
for
f
o
r
Division
D
i
v
i
s
i
o
n
2).
2
)
.
4.3.9.
4
.
3
.
9
.
The
T
h
e
circumferential
c
i
r
c
u
m
f
e
r
e
n
t
i
a
l
weld
w
e
l
d
of
o
f
Ring-Type
R
i
n
g
-
T
y
p
e
Girth
G
i
r
t
h
Flanges
F
l
a
n
g
e
s
designed
d
e
s
i
g
n
e
d
and
a
n
d
fabricated
f
a
b
r
i
c
a
t
e
d
according
a
c
c
o
r
d
i
n
g
to
t
o
Appendix
A
p
p
e
n
d
i
x
2,
2
,
Figure
F
i
g
u
r
e
(11)
(
1
1
)
of
o
f
ASME
A
S
M
E
Code
C
o
d
e
shall
s
h
a
l
l
be
b
e
UT
U
T
examined.
e
x
a
m
i
n
e
d
.
4.3.10.
4
.
3
.
1
0
.
Heat
H
e
a
t
exchanger
e
x
c
h
a
n
g
e
r
guarantee
g
u
a
r
a
n
t
e
e
shall
s
h
a
l
l
include
i
n
c
l
u
d
e
thermal
t
h
e
r
m
a
l
and
a
n
d
mechanical
m
e
c
h
a
n
i
c
a
l
performances.
p
e
r
f
o
r
m
a
n
c
e
s
.
4.3.11.
4
.
3
.
1
1
.
In
I
n
case
c
a
s
e
of
o
f
heat
h
e
a
t
exchangers
e
x
c
h
a
n
g
e
r
s
located
l
o
c
a
t
e
d
at
a
t
elevation
e
l
e
v
a
t
i
o
n
upper
u
p
p
e
r
than
t
h
a
n
3
3
meters
m
e
t
e
r
s
shall
s
h
a
l
l
be
b
e
provided
p
r
o
v
i
d
e
d
extra
e
x
t
r
a
facilities
f
a
c
i
l
i
t
i
e
s
to
t
o
easy
e
a
s
y
removal
r
e
m
o
v
a
l
of
o
f
the
t
h
e
tube
t
u
b
e
bundle.
b
u
n
d
l
e
.
4.3.12.
4
.
3
.
1
2
.
When
W
h
e
n
the
t
h
e
tube
t
u
b
e
to
t
o
tube-sheet
t
u
b
e
-
s
h
e
e
t
joints
j
o
i
n
t
s
are
a
r
e
specified
s
p
e
c
i
f
i
e
d
for
f
o
r
full
f
u
l
l
strength
s
t
r
e
n
g
t
h
welding,
w
e
l
d
i
n
g
,
the
t
h
e
full
f
u
l
l
strength
s
t
r
e
n
g
t
h
weld
w
e
l
d
shall
s
h
a
l
l
be
b
e
specified
s
p
e
c
i
f
i
e
d
and
a
n
d
calculated
c
a
l
c
u
l
a
t
e
d
in
i
n
accordance
a
c
c
o
r
d
a
n
c
e
with
w
i
t
h
paragraph
p
a
r
a
g
r
a
p
h
UW-20.4
U
W
-
2
0
.
4
of
o
f
ASME
A
S
M
E
BPVC
B
P
V
C
Section
S
e
c
t
i
o
n
VIII
V
I
I
I
Division
D
i
v
i
s
i
o
n
1.
1
.
The
T
h
e
tube
t
u
b
e
to
t
o
tubesheet
t
u
b
e
s
h
e
e
t
joint
j
o
i
n
t
welds
w
e
l
d
s
shall
s
h
a
l
l
be
b
e
leak
l
e
a
k
tested
t
e
s
t
e
d
(leak
(
l
e
a
k
tightness)
t
i
g
h
t
n
e
s
s
)
as
a
s
per
p
e
r
EEMUA
E
E
M
U
A
Pub
P
u
b
143,
1
4
3
,
item
i
t
e
m
12.4
1
2
.
4
(Freon).
(
F
r
e
o
n
)
.
The
T
h
e
manufacturer
m
a
n
u
f
a
c
t
u
r
e
r
shall
s
h
a
l
l
also
a
l
s
o
provide
p
r
o
v
i
d
e
the
t
h
e
test
t
e
s
t
procedure.
p
r
o
c
e
d
u
r
e
.
4.3.13.
4
.
3
.
1
3
.
The
T
h
e
stud,
s
t
u
d
,
bolts
b
o
l
t
s
and
a
n
d
nuts
n
u
t
s
of
o
f
heat
h
e
a
t
exchanger
e
x
c
h
a
n
g
e
r
girth
g
i
r
t
h
flanges
f
l
a
n
g
e
s
shall
s
h
a
l
l
comply
c
o
m
p
l
y
with
w
i
t
h
applicable
a
p
p
l
i
c
a
b
l
e
piping
p
i
p
i
n
g
specification
s
p
e
c
i
f
i
c
a
t
i
o
n
for
f
o
r
equipment
e
q
u
i
p
m
e
n
t
nozzles.
n
o
z
z
l
e
s
.
A
A
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
AREA:
A
R
E
A
:
TITLE:
T
I
T
L
E
:
4.4.
4
.
4
.
Wind
W
i
n
d
Loads
L
o
a
d
s
TECHNICAL
T
E
C
H
N
I
C
A
L
SPECIFICATION
S
P
E
C
I
F
I
C
A
T
I
O
N
N
N
O
O
I-ET-5230.00-2221-500-APJ-001
I
-
E
T
-
5
2
3
0
.
0
0
-
2
2
2
1
-
5
0
0
-
A
P
J
-
0
0
1
U-1250
U
-
1
2
5
0
DESIGN
D
E
S
I
G
N
CRITERIA
C
R
I
T
E
R
I
A
–
–
STATIC
S
T
A
T
I
C
EQUIPMENT
E
Q
U
I
P
M
E
N
T
D-591
D
-
5
9
1
AND
A
N
D
E-590
E
-
5
9
0
SHEET:
S
H
E
E
T
:
REV.
R
E
V
.
8
8
of
o
f
9
9
SRGE/SI-IV/IES
S
R
G
E
/
S
I
-
I
V
/
I
E
S
INTERNA
I
N
T
E
R
N
A
4.4.1.
4
.
4
.
1
.
Wind
W
i
n
d
loads
l
o
a
d
s
on
o
n
the
t
h
e
equipment
e
q
u
i
p
m
e
n
t
shall
s
h
a
l
l
be
b
e
calculated
c
a
l
c
u
l
a
t
e
d
by
b
y
using
u
s
i
n
g
the
t
h
e
PETROBRAS
P
E
T
R
O
B
R
A
S
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
I-ET-0000.00-0000-500-PEI-004
I
-
E
T
-
0
0
0
0
.
0
0
-
0
0
0
0
-
5
0
0
-
P
E
I
-
0
0
4
and
a
n
d
the
t
h
e
Brazilian
B
r
a
z
i
l
i
a
n
Standard
S
t
a
n
d
a
r
d
ABNT
A
B
N
T
NBR-6123.
N
B
R
-
6
1
2
3
.
4.5.
4
.
5
.
NR-13
N
R
-
1
3
Requirements
R
e
q
u
i
r
e
m
e
n
t
s
4.5.1.
4
.
5
.
1
.
The
T
h
e
CONTRACTOR
C
O
N
T
R
A
C
T
O
R
shall
s
h
a
l
l
comply
c
o
m
p
l
y
with
w
i
t
h
the
t
h
e
Brazilian
B
r
a
z
i
l
i
a
n
Ministry
M
i
n
i
s
t
r
y
of
o
f
Labor
L
a
b
o
r
Regulation
R
e
g
u
l
a
t
i
o
n
no.
n
o
.
NR-13
N
R
-
1
3
requirements,
r
e
q
u
i
r
e
m
e
n
t
s
,
according
a
c
c
o
r
d
i
n
g
to
t
o
the
t
h
e
Technical
T
e
c
h
n
i
c
a
l
Specifications
S
p
e
c
i
f
i
c
a
t
i
o
n
s
I-ET-0000.00-0000-500-
I
-
E
T
-
0
0
0
0
.
0
0
-
0
0
0
0
-
5
0
0
-
PEI-001
P
E
I
-
0
0
1
and
a
n
d
ET-0000.00-0000-510-PEI-001,
E
T
-
0
0
0
0
.
0
0
-
0
0
0
0
-
5
1
0
-
P
E
I
-
0
0
1
,
through
t
h
r
o
u
g
h
the
t
h
e
production
p
r
o
d
u
c
t
i
o
n
and
a
n
d
organization
o
r
g
a
n
i
z
a
t
i
o
n
of
o
f
the
t
h
e
necessary
n
e
c
e
s
s
a
r
y
technical
t
e
c
h
n
i
c
a
l
documentation
d
o
c
u
m
e
n
t
a
t
i
o
n
(Manuals,
(
M
a
n
u
a
l
s
,
Reports,
R
e
p
o
r
t
s
,
Installation,
I
n
s
t
a
l
l
a
t
i
o
n
,
Design,
D
e
s
i
g
n
,
etc.)
e
t
c
.
)
required
r
e
q
u
i
r
e
d
in
i
n
the
t
h
e
Technical
T
e
c
h
n
i
c
a
l
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
above.
a
b
o
v
e
.
This
T
h
i
s
job
j
o
b
shall
s
h
a
l
l
be
b
e
performed
p
e
r
f
o
r
m
e
d
by
b
y
the
t
h
e
Licensed
L
i
c
e
n
s
e
d
Professional
P
r
o
f
e
s
s
i
o
n
a
l
approved
a
p
p
r
o
v
e
d
by
b
y
PETROBRAS.
P
E
T
R
O
B
R
A
S
.
4.6.
4
.
6
.
Equipment
E
q
u
i
p
m
e
n
t
Subject
S
u
b
j
e
c
t
to
t
o
H2S
H
2
S
Service
S
e
r
v
i
c
e
4.6.1.
4
.
6
.
1
.
Equipment
E
q
u
i
p
m
e
n
t
subject
s
u
b
j
e
c
t
to
t
o
H2S
H
2
S
Service
S
e
r
v
i
c
e
shall
s
h
a
l
l
comply
c
o
m
p
l
y
with
w
i
t
h
the
t
h
e
requirements
r
e
q
u
i
r
e
m
e
n
t
s
of
o
f
the
t
h
e
PETROBRAS
P
E
T
R
O
B
R
A
S
Standard
S
t
a
n
d
a
r
d
NI-1706.
N
I
-
1
7
0
6
.
4.7.
4
.
7
.
Stress
S
t
r
e
s
s
Analysis
A
n
a
l
y
s
i
s
by
b
y
the
t
h
e
Finite
F
i
n
i
t
e
Element
E
l
e
m
e
n
t
Method
M
e
t
h
o
d
4.7.1.
4
.
7
.
1
.
The
T
h
e
requirements
r
e
q
u
i
r
e
m
e
n
t
s
of
o
f
Stress
S
t
r
e
s
s
Analysis
A
n
a
l
y
s
i
s
by
b
y
the
t
h
e
Finite
F
i
n
i
t
e
Element
E
l
e
m
e
n
t
Method
M
e
t
h
o
d
shall
s
h
a
l
l
be
b
e
according
a
c
c
o
r
d
i
n
g
to
t
o
PETROBRAS
P
E
T
R
O
B
R
A
S
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
I-ET-0000.00-0000-500-PEI-003
I
-
E
T
-
0
0
0
0
.
0
0
-
0
0
0
0
-
5
0
0
-
P
E
I
-
0
0
3
(Procedure
(
P
r
o
c
e
d
u
r
e
for
f
o
r
Performing
P
e
r
f
o
r
m
i
n
g
Stress
S
t
r
e
s
s
Analysis
A
n
a
l
y
s
i
s
by
b
y
Means
M
e
a
n
s
of
o
f
Finite
F
i
n
i
t
e
Element
E
l
e
m
e
n
t
Method)
M
e
t
h
o
d
)
and
a
n
d
paragraph
p
a
r
a
g
r
a
p
h
5.4
5
.
4
of
o
f
N-266.
N
-
2
6
6
.
4.8.
4
.
8
.
Loads
L
o
a
d
s
on
o
n
Nozzles
N
o
z
z
l
e
s
and
a
n
d
Clips
C
l
i
p
s
4.8.1.
4
.
8
.
1
.
The
T
h
e
local
l
o
c
a
l
stresses
s
t
r
e
s
s
e
s
on
o
n
nozzles
n
o
z
z
l
e
s
due
d
u
e
to
t
o
external
e
x
t
e
r
n
a
l
loads
l
o
a
d
s
shall
s
h
a
l
l
be
b
e
according
a
c
c
o
r
d
i
n
g
to
t
o
PETROBRAS
P
E
T
R
O
B
R
A
S
Specification
S
p
e
c
i
f
i
c
a
t
i
o
n
I-ET-0000.00-0000-500-PEI-005
I
-
E
T
-
0
0
0
0
.
0
0
-
0
0
0
0
-
5
0
0
-
P
E
I
-
0
0
5
(Maximum
(
M
a
x
i
m
u
m
Allowable
A
l
l
o
w
a
b
l
e
Loads
L
o
a
d
s
on
o
n
Pressure
P
r
e
s
s
u
r
e
Vessel
V
e
s
s
e
l
Nozzles).
N
o
z
z
l
e
s
)
.
Alternatively,
A
l
t
e
r
n
a
t
i
v
e
l
y
,
the
t
h
e
use
u
s
e
of
o
f
Finite
F
i
n
i
t
e
Element
E
l
e
m
e
n
t
Method
M
e
t
h
o
d
for
f
o
r
stress
s
t
r
e
s
s
evaluation
e
v
a
l
u
a
t
i
o
n
is
i
s
allowed,
a
l
l
o
w
e
d
,
according
a
c
c
o
r
d
i
n
g
to
t
o
the
t
h
e
item
i
t
e
m
3.14
3
.
1
4
requirements.
r
e
q
u
i
r
e
m
e
n
t
s
.
4.9.
4
.
9
.
Anchor
A
n
c
h
o
r
Bolts
B
o
l
t
s
4.9.1.
4
.
9
.
1
.
The
T
h
e
resistant
r
e
s
i
s
t
a
n
t
area
a
r
e
a
to
t
o
be
b
e
considered
c
o
n
s
i
d
e
r
e
d
in
i
n
the
t
h
e
calculation
c
a
l
c
u
l
a
t
i
o
n
of
o
f
the
t
h
e
anchor
a
n
c
h
o
r
bolts
b
o
l
t
s
to
t
o
pressure
p
r
e
s
s
u
r
e
vessels
v
e
s
s
e
l
s
shall
s
h
a
l
l
be
b
e
the
t
h
e
minor
m
i
n
o
r
valued
v
a
l
u
e
d
between
b
e
t
w
e
e
n
the
t
h
e
root
r
o
o
t
area
a
r
e
a
(threaded
(
t
h
r
e
a
d
e
d
part)
p
a
r
t
)
and
a
n
d
the
t
h
e
corroded
c
o
r
r
o
d
e
d
part
p
a
r
t
(external
(
e
x
t
e
r
n
a
l
diameter
d
i
a
m
e
t
e
r
minus
m
i
n
u
s
corrosion
c
o
r
r
o
s
i
o
n
allowance
a
l
l
o
w
a
n
c
e
of
o
f
the
t
h
e
anchor
a
n
c
h
o
r
bolt).
b
o
l
t
)
.
4.9.2.
4
.
9
.
2
.
The
T
h
e
corrosion
c
o
r
r
o
s
i
o
n
allowance
a
l
l
o
w
a
n
c
e
to
t
o
be
b
e
considered
c
o
n
s
i
d
e
r
e
d
shall
s
h
a
l
l
be
b
e
2.0
2
.
0
mm
m
m
on
o
n
the
t
h
e
radius
r
a
d
i
u
s
of
o
f
the
t
h
e
anchor
a
n
c
h
o
r
bolt.
b
o
l
t
.
4.9.3.
4
.
9
.
3
.
When
W
h
e
n
not
n
o
t
previously
p
r
e
v
i
o
u
s
l
y
specified,
s
p
e
c
i
f
i
e
d
,
the
t
h
e
material
m
a
t
e
r
i
a
l
for
f
o
r
the
t
h
e
anchor
a
n
c
h
o
r
bolt
b
o
l
t
shall
s
h
a
l
l
be
b
e
ASTM-F-1554
A
S
T
M
-
F
-
1
5
5
4
Grade
G
r
a
d
e
36
3
6
(formerly
(
f
o
r
m
e
r
l
y
ASTM
A
S
T
M
A
A
307
3
0
7
Grade
G
r
a
d
e
C).
C
)
.
4.10.
4
.
1
0
.
Insulation
I
n
s
u
l
a
t
i
o
n
Requirements
R
e
q
u
i
r
e
m
e
n
t
s
4.10.1.
4
.
1
0
.
1
.
Vessel
V
e
s
s
e
l
D-591
D
-
5
9
1
shall
s
h
a
l
l
not
n
o
t
have
h
a
v
e
thermal
t
h
e
r
m
a
l
insulation.
i
n
s
u
l
a
t
i
o
n
.
4.10.2.
4
.
1
0
.
2
.
Heat
H
e
a
t
Exchanger
E
x
c
h
a
n
g
e
r
E-590:
E
-
5
9
0
:
-
Shell
S
h
e
l
l
side:
s
i
d
e
:
Personal
P
e
r
s
o
n
a
l
protection.
p
r
o
t
e
c
t
i
o
n
.
-
Tube
T
u
b
e
side:
s
i
d
e
:
No
N
o
thermal
t
h
e
r
m
a
l
insulation
i
n
s
u
l
a
t
i
o
n
4.11.
4
.
1
1
.
Painting
P
a
i
n
t
i
n
g
Requirements
R
e
q
u
i
r
e
m
e
n
t
s
4.11.1.
4
.
1
1
.
1
.
Equipment
E
q
u
i
p
m
e
n
t
surfaces
s
u
r
f
a
c
e
s
with
w
i
t
h
thermal
t
h
e
r
m
a
l
insulation
i
n
s
u
l
a
t
i
o
n
shall
s
h
a
l
l
be
b
e
coated
c
o
a
t
e
d
in
i
n
accordance
a
c
c
o
r
d
a
n
c
e
with
w
i
t
h
PETROBRAS
P
E
T
R
O
B
R
A
S
procedure
p
r
o
c
e
d
u
r
e
N-0002P,
N
-
0
0
0
2
P
,
under
u
n
d
e
r
condition
c
o
n
d
i
t
i
o
n
7.
7
.
4.11.2.
4
.
1
1
.
2
.
Equipment
E
q
u
i
p
m
e
n
t
surfaces
s
u
r
f
a
c
e
s
without
w
i
t
h
o
u
t
thermal
t
h
e
r
m
a
l
insulation
i
n
s
u
l
a
t
i
o
n
shall
s
h
a
l
l
be
b
e
coated
c
o
a
t
e
d
in
i
n
compliance
c
o
m
p
l
i
a
n
c
e
with
w
i
t
h
PETROBRAS
P
E
T
R
O
B
R
A
S
procedure
p
r
o
c
e
d
u
r
e
N-0002P,
N
-
0
0
0
2
P
,
under
u
n
d
e
r
condition
c
o
n
d
i
t
i
o
n
1.
1
.
A
A
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AREA:
A
R
E
A
:
TITLE:
T
I
T
L
E
:
TECHNICAL
T
E
C
H
N
I
C
A
L
SPECIFICATION
S
P
E
C
I
F
I
C
A
T
I
O
N
N
N
O
O
I-ET-5230.00-2221-500-APJ-001
I
-
E
T
-
5
2
3
0
.
0
0
-
2
2
2
1
-
5
0
0
-
A
P
J
-
0
0
1
U-1250
U
-
1
2
5
0
DESIGN
D
E
S
I
G
N
CRITERIA
C
R
I
T
E
R
I
A
–
–
STATIC
S
T
A
T
I
C
EQUIPMENT
E
Q
U
I
P
M
E
N
T
D-591
D
-
5
9
1
AND
A
N
D
E-590
E
-
5
9
0
SHEET:
S
H
E
E
T
:
REV.
R
E
V
.
9
9
of
o
f
9
9
SRGE/SI-IV/IES
S
R
G
E
/
S
I
-
I
V
/
I
E
S
INTERNA
I
N
T
E
R
N
A
A
A
A
A
-
-
Reference
R
e
f
e
r
e
n
c
e
point
p
o
i
n
t
for
f
o
r
location
l
o
c
a
t
i
o
n
of
o
f
nozzles.
n
o
z
z
l
e
s
.
B
B
-
-
Reference
R
e
f
e
r
e
n
c
e
point
p
o
i
n
t
for
f
o
r
location
l
o
c
a
t
i
o
n
of
o
f
saddles.
s
a
d
d
l
e
s
.
C
C
-
-
Reference
R
e
f
e
r
e
n
c
e
point
p
o
i
n
t
for
f
o
r
location
l
o
c
a
t
i
o
n
of
o
f
nozzles
n
o
z
z
l
e
s
in
i
n
the
t
h
e
head
h
e
a
d
or
o
r
cover.
c
o
v
e
r
.
R
R
-
-
Horizontal
H
o
r
i
z
o
n
t
a
l
reference
r
e
f
e
r
e
n
c
e
line.
l
i
n
e
.
a
a
-
-
Level
L
e
v
e
l
for
f
o
r
nozzles.
n
o
z
z
l
e
s
.
b
b
-
-
Level
L
e
v
e
l
for
f
o
r
saddles.
s
a
d
d
l
e
s
.
d
d
-
-
Level
L
e
v
e
l
for
f
o
r
nozzles
n
o
z
z
l
e
s
in
i
n
head
h
e
a
d
or
o
r
cover.
c
o
v
e
r
.
e,
e
,
h,
h
,
i
i
-
-
Level
L
e
v
e
l
for
f
o
r
instrument
i
n
s
t
r
u
m
e
n
t
nozzles.
n
o
z
z
l
e
s
.
f,
f
,
g
g
-
-
Level
L
e
v
e
l
for
f
o
r
mouth
m
o
u
t
h
of
o
f
vessel.
v
e
s
s
e
l
.
�
-
-
Slope
S
l
o
p
e
of
o
f
vessel.
v
e
s
s
e
l
.
*
*
-
-
Refers
R
e
f
e
r
s
to
t
o
all
a
l
l
points
p
o
i
n
t
s
of
o
f
nozzles.
n
o
z
z
l
e
s
.
FIGURE
F
I
G
U
R
E
1
1
DIAGRAM
D
I
A
G
R
A
M
SHOWING
S
H
O
W
I
N
G
LOCATION
L
O
C
A
T
I
O
N
OF
O
F
NOZZLES
N
O
Z
Z
L
E
S
ON
O
N
VESSELS
V
E
S
S
E
L
S
WITH
W
I
T
H
SLOPE
S
L
O
P
E
FOR
F
O
R
REFERENCE
R
E
F
E
R
E
N
C
E
ONLY
O
N
L
Y
0.00
0.00
0.00
1.00
0.00
0.00