m0lzf
2026-06-05T16:22:25+02:00
Microsoft® Excel® 2016
2026-06-09T17:31:37+02:00
Microsoft® Excel® 2016
Microsoft® Excel® 2016
Microsoft® Excel® 2016
2026-06-05T16:22:25+02:00
2026-06-09T17:31:37+02:00
m0lzf
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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}
Air
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2
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Air
A
i
r
Liquide
L
i
q
u
i
d
e
Confidential
C
o
n
f
i
d
e
n
t
i
a
l
Information
I
n
f
o
r
m
a
t
i
o
n
This
T
h
i
s
print
p
r
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n
t
is
i
s
the
t
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property
p
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o
p
e
r
t
y
of
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f
L’Air
L
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A
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L
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q
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d
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S.A.
S
.
A
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and
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indirect)
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and
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this
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Rev.
R
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v
.
1,
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issued
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26-Jun-18
2
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h
y
s
i
c
a
l
characteristics
c
h
a
r
a
c
t
e
r
i
s
t
i
c
s
7
7
16
1
6
17
1
7
PROCESS
P
R
O
C
E
S
S
DESCRIPTION
D
E
S
C
R
I
P
T
I
O
N
AND
A
N
D
VENDOR
V
E
N
D
O
R
SCOPE
S
C
O
P
E
OF
O
F
SUPPLY
S
U
P
P
L
Y
18
1
8
19
1
9
20
2
0
PROCESS
P
R
O
C
E
S
S
SCHEME
S
C
H
E
M
E
21
2
1
22
2
2
23
2
3
24
2
4
25
2
5
26
2
6
27
2
7
28
2
8
29
2
9
30
3
0
Ho
H
o
31
3
1
32
3
2
33
3
3
PROCESS
P
R
O
C
E
S
S
DESCIPTION
D
E
S
C
I
P
T
I
O
N
34
3
4
35
3
5
The
T
h
e
WET
W
E
T
FLUE
F
L
U
E
GAS
G
A
S
COMPRESSOR
C
O
M
P
R
E
S
S
O
R
(C12)
(
C
1
2
)
compresses
c
o
m
p
r
e
s
s
e
s
wet
w
e
t
flue
f
l
u
e
gas
g
a
s
from
f
r
o
m
low
l
o
w
to
t
o
medium
m
e
d
i
u
m
pressure
p
r
e
s
s
u
r
e
and
a
n
d
is
i
s
divided
d
i
v
i
d
e
d
into
i
n
t
o
two
t
w
o
sections.
s
e
c
t
i
o
n
s
.
36
3
6
The
T
h
e
WET
W
E
T
FLUE
F
L
U
E
GAS
G
A
S
contains
c
o
n
t
a
i
n
s
acidic
a
c
i
d
i
c
components
c
o
m
p
o
n
e
n
t
s
(e.g
(
e
.
g
HNO3,
H
N
O
3
,
H2SO4)
H
2
S
O
4
)
that
t
h
a
t
can
c
a
n
condense
c
o
n
d
e
n
s
e
in
i
n
the
t
h
e
intercooler
i
n
t
e
r
c
o
o
l
e
r
of
o
f
section
s
e
c
t
i
o
n
1
1
of
o
f
the
t
h
e
37
3
7
compressor;
c
o
m
p
r
e
s
s
o
r
;
vendor
v
e
n
d
o
r
to
t
o
advise
a
d
v
i
s
e
on
o
n
material
m
a
t
e
r
i
a
l
selection.
s
e
l
e
c
t
i
o
n
.
38
3
8
Section
S
e
c
t
i
o
n
2
2
is
i
s
adiabatic
a
d
i
a
b
a
t
i
c
in
i
n
order
o
r
d
e
r
to
t
o
recover
r
e
c
o
v
e
r
heat
h
e
a
t
at
a
t
the
t
h
e
compressor
c
o
m
p
r
e
s
s
o
r
discharge
d
i
s
c
h
a
r
g
e
with
w
i
t
h
a
a
heat
h
e
a
t
recovery
r
e
c
o
v
e
r
y
system
s
y
s
t
e
m
(outside
(
o
u
t
s
i
d
e
vendor
v
e
n
d
o
r
scope
s
c
o
p
e
of
o
f
39
3
9
supply).
s
u
p
p
l
y
)
.
This
T
h
i
s
heat
h
e
a
t
will
w
i
l
l
be
b
e
used
u
s
e
d
to
t
o
preheat
p
r
e
h
e
a
t
the
t
h
e
gas
g
a
s
going
g
o
i
n
g
through
t
h
r
o
u
g
h
the
t
h
e
expander
e
x
p
a
n
d
e
r
side
s
i
d
e
of
o
f
the
t
h
e
compander
c
o
m
p
a
n
d
e
r
of
o
f
the
t
h
e
plant,
p
l
a
n
t
,
see
s
e
e
below
b
e
l
o
w
scheme.
s
c
h
e
m
e
.
Compressor
C
o
m
p
r
e
s
s
o
r
discharge
d
i
s
c
h
a
r
g
e
temperature
t
e
m
p
e
r
a
t
u
r
e
will
w
i
l
l
then
t
h
e
n
be
b
e
calculated
c
a
l
c
u
l
a
t
e
d
according
a
c
c
o
r
d
i
n
g
to
t
o
needed
n
e
e
d
e
d
temperature
t
e
m
p
e
r
a
t
u
r
e
at
a
t
the
t
h
e
inlet
i
n
l
e
t
of
o
f
the
t
h
e
expander,
e
x
p
a
n
d
e
r
,
40
4
0
see
s
e
e
design
d
e
s
i
g
n
philosophy
p
h
i
l
o
s
o
p
h
y
page
p
a
g
e
5
5
and
a
n
d
6.
6
.
41
4
1
This
T
h
i
s
datasheet
d
a
t
a
s
h
e
e
t
contains
c
o
n
t
a
i
n
s
the
t
h
e
process
p
r
o
c
e
s
s
specifications
s
p
e
c
i
f
i
c
a
t
i
o
n
s
for
f
o
r
DESIGN,
D
E
S
I
G
N
,
NOMINAL,
N
O
M
I
N
A
L
,
TURNDOWN
T
U
R
N
D
O
W
N
and
a
n
d
START-UP
S
T
A
R
T
-
U
P
cases.
c
a
s
e
s
.
42
4
2
Vendor
V
e
n
d
o
r
to
t
o
optimize
o
p
t
i
m
i
z
e
the
t
h
e
compressor
c
o
m
p
r
e
s
s
o
r
operation
o
p
e
r
a
t
i
o
n
and
a
n
d
TCO
T
C
O
considering
c
o
n
s
i
d
e
r
i
n
g
all
a
l
l
cases
c
a
s
e
s
and
a
n
d
power
p
o
w
e
r
evaluation.
e
v
a
l
u
a
t
i
o
n
.
43
4
3
Heat
H
e
a
t
integration
i
n
t
e
g
r
a
t
i
o
n
is
i
s
performed
p
e
r
f
o
r
m
e
d
on
o
n
the
t
h
e
first
f
i
r
s
t
stage
s
t
a
g
e
intercooler,
i
n
t
e
r
c
o
o
l
e
r
,
pressure
p
r
e
s
s
u
r
e
ratio
r
a
t
i
o
to
t
o
be
b
e
chosen
c
h
o
s
e
n
to
t
o
reach
r
e
a
c
h
specified
s
p
e
c
i
f
i
e
d
temperature
t
e
m
p
e
r
a
t
u
r
e
at
a
t
44
4
4
the
t
h
e
inlet
i
n
l
e
t
of
o
f
intercooler.
i
n
t
e
r
c
o
o
l
e
r
.
45
4
5
Vendor
V
e
n
d
o
r
to
t
o
advise
a
d
v
i
s
e
the
t
h
e
number
n
u
m
b
e
r
of
o
f
compression
c
o
m
p
r
e
s
s
i
o
n
stages
s
t
a
g
e
s
and
a
n
d
intercoolers
i
n
t
e
r
c
o
o
l
e
r
s
in
i
n
both
b
o
t
h
sections.
s
e
c
t
i
o
n
s
.
46
4
6
Vendor
V
e
n
d
o
r
to
t
o
advise
a
d
v
i
s
e
the
t
h
e
sealing
s
e
a
l
i
n
g
gas
g
a
s
configuration.
c
o
n
f
i
g
u
r
a
t
i
o
n
.
47
4
7
48
4
8
49
4
9
HOT
H
O
T
WATER
W
A
T
E
R
SYSTEM
S
Y
S
T
E
M
Cold
C
o
l
d
water
w
a
t
e
r
Hot
H
o
t
water
w
a
t
e
r
50
5
0
51
5
1
52
5
2
53
5
3
54
5
4
GAS
G
A
S
FEED
F
E
E
D
FG
F
G
Compressor
C
o
m
p
r
e
s
s
o
r
PROCESS
P
R
O
C
E
S
S
C39
C
3
9
Expander
E
x
p
a
n
d
e
r
Line
L
i
n
e
revised
r
e
v
i
s
e
d
under
u
n
d
e
r
Rev.
R
e
v
.
No.
N
o
.
Project
P
r
o
j
e
c
t
No.
N
o
.
Document
D
o
c
u
m
e
n
t
No.
N
o
.
Sheet
S
h
e
e
t
/
/
of
o
f
53573
5
3
5
7
3
53573-62-01-PR-013712
5
3
5
7
3
-
6
2
-
0
1
-
P
R
-
0
1
3
7
1
2
2
2
/
/
7
7
Printed
P
r
i
n
t
e
d
by
b
y
/
/
date
d
a
t
e
/
/
time:
t
i
m
e
:
N/A
N
/
A
/
/
28/02/23
2
8
/
0
2
/
2
3
2
2
2
2
2
2
2
2
2
2
2
2
Revision
R
e
v
i
s
i
o
n
2
2
/
/
11:07
1
1
:
0
7
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Air
A
i
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Liquide
L
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i
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Confidential
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This
T
h
i
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print
p
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is
i
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the
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h
e
property
p
r
o
p
e
r
t
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of
o
f
L’Air
L
’
A
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Liquide
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S.A.
S
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A
.
or
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.
Copyright
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o
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h
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a
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recipient
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p
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n
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to
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o
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a
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t
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●INTERNAL
●
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N
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E
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N
A
L
Derived
D
e
r
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d
from
f
r
o
m
G-TPL-13-0-1,
G
-
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P
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1
3
-
0
-
1
,
Rev.
R
e
v
.
1,
1
,
issued
i
s
s
u
e
d
26-Jun-18
2
6
-
J
u
n
-
1
8
party,
p
a
r
t
y
,
reproduced,
r
e
p
r
o
d
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c
e
d
,
copied,
c
o
p
i
e
d
,
lent,
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i
s
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or
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d
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,
nor
n
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r
used
u
s
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d
for
f
o
r
any
a
n
y
purpose
p
u
r
p
o
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e
other
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t
h
e
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than
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a
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for
f
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it
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expressly
e
x
p
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s
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Rev.
R
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furnished.
f
u
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.
This
T
h
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s
print
p
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t
is
i
s
lent
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e
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subject
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u
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.
AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR
A
L
_
C
R
Y
O
_
P
R
O
C
E
S
S
_
D
S
_
T
E
M
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C
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M
P
R
E
S
S
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R
01
0
1
Item
I
t
e
m
Number
N
u
m
b
e
r
02
0
2
621001C12
6
2
1
0
0
1
C
1
2
03
0
3
Designation
D
e
s
i
g
n
a
t
i
o
n
PROCESS
P
R
O
C
E
S
S
DATA
D
A
T
A
-
-
WET
W
E
T
FEED
F
E
E
D
GAS
G
A
S
COMPRESSOR
C
O
M
P
R
E
S
S
O
R
04
0
4
05
0
5
Number
N
u
m
b
e
r
required
r
e
q
u
i
r
e
d
1
1
Supplier/Type
S
u
p
p
l
i
e
r
/
T
y
p
e
06
0
6
Driver
D
r
i
v
e
r
Electrical
E
l
e
c
t
r
i
c
a
l
Motor
M
o
t
o
r
07
0
7
RATED
R
A
T
E
D
NOMINAL
N
O
M
I
N
A
L
NOMINAL
N
O
M
I
N
A
L
CASE
C
A
S
E
START
S
T
A
R
T
UP
U
P
08
0
8
DESIGN
D
E
S
I
G
N
WINTER
W
I
N
T
E
R
SUMMER
S
U
M
M
E
R
09
0
9
Fluid
F
l
u
i
d
(see
(
s
e
e
page
p
a
g
e
5
5
for
f
o
r
detailed
d
e
t
a
i
l
e
d
composition
c
o
m
p
o
s
i
t
i
o
n
and
a
n
d
properties)
p
r
o
p
e
r
t
i
e
s
)
Flue
F
l
u
e
gas
g
a
s
Flue
F
l
u
e
gas
g
a
s
Flue
F
l
u
e
gas
g
a
s
Air
A
i
r
10
1
0
SUCTION
S
U
C
T
I
O
N
11
1
1
Molar
M
o
l
a
r
Flowrate
F
l
o
w
r
a
t
e
(wet
(
w
e
t
basis)
b
a
s
i
s
)
Nm
N
m
3
3
/h
/
h
601
6
0
1
413
4
1
3
552
5
5
2
936
9
3
6
545
5
4
5
230
2
3
0
2
2
12
1
2
Mass
M
a
s
s
Flowrate
F
l
o
w
r
a
t
e
(wet
(
w
e
t
basis)
b
a
s
i
s
)
kg/h
k
g
/
h
835
8
3
5
595
5
9
5
767
7
6
7
768
7
6
8
761
7
6
1
551
5
5
1
2
2
13
1
3
Volume
V
o
l
u
m
e
Flowrate
F
l
o
w
r
a
t
e
m
m
3
3
/h
/
h
693
6
9
3
721
7
2
1
637
6
3
7
797
7
9
7
615
6
1
5
487
4
8
7
2
2
14
1
4
Inlet
I
n
l
e
t
Pressure
P
r
e
s
s
u
r
e
(1)
(
1
)
bar(a)
b
a
r
(
a
)
0.990
0
.
9
9
0
0.990
0
.
9
9
0
0.990
0
.
9
9
0
1.013
1
.
0
1
3
2
2
15
1
5
Temperature
T
e
m
p
e
r
a
t
u
r
e
(1)
(
1
)
°C
°
C
35.0
3
5
.
0
35.0
3
5
.
0
28.4
2
8
.
4
23.8
2
3
.
8
2
2
16
1
6
Duct
D
u
c
t
diameter
d
i
a
m
e
t
e
r
DN
D
N
146"
1
4
6
"
2
2
17
1
7
Design
D
e
s
i
g
n
pressure
p
r
e
s
s
u
r
e
min.
m
i
n
.
/
/
max.
m
a
x
.
mbarg
m
b
a
r
g
-0.09
-
0
.
0
9
/
/
+0.09
+
0
.
0
9
2
2
18
1
8
Design
D
e
s
i
g
n
temperature
t
e
m
p
e
r
a
t
u
r
e
min.
m
i
n
.
/
/
max.
m
a
x
.
°C
°
C
-20
-
2
0
/
/
+80
+
8
0
2
2
19
1
9
20
2
0
Section
S
e
c
t
i
o
n
1
1
DISCHARGE
D
I
S
C
H
A
R
G
E
(before
(
b
e
f
o
r
e
intercooler)
i
n
t
e
r
c
o
o
l
e
r
)
(6)
(
6
)
21
2
1
Section
S
e
c
t
i
o
n
1
1
discharge
d
i
s
c
h
a
r
g
e
pressure
p
r
e
s
s
u
r
e
bar(a)
b
a
r
(
a
)
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
22
2
2
Section
S
e
c
t
i
o
n
1
1
discharge
d
i
s
c
h
a
r
g
e
temperature
t
e
m
p
e
r
a
t
u
r
e
(2)
(
2
)
°C
°
C
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
2
2
23
2
3
Section
S
e
c
t
i
o
n
2
2
DISCHARGE
D
I
S
C
H
A
R
G
E
24
2
4
Molar
M
o
l
a
r
Flowrate
F
l
o
w
r
a
t
e
(wet
(
w
e
t
basis)
b
a
s
i
s
)
(3)
(
3
)
Nm
N
m
3
3
/h
/
h
v.t.g
v
.
t
.
g
v.t.g
v
.
t
.
g
v.t.g
v
.
t
.
g
25
2
5
Mass
M
a
s
s
Flowrate
F
l
o
w
r
a
t
e
(wet
(
w
e
t
basis)
b
a
s
i
s
)
kg/h
k
g
/
h
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
26
2
6
Section
S
e
c
t
i
o
n
2
2
discharge
d
i
s
c
h
a
r
g
e
pressure
p
r
e
s
s
u
r
e
bar(a)
b
a
r
(
a
)
8.60
8
.
6
0
8.27
8
.
2
7
8.27
8
.
2
7
2
2
27
2
7
Temperature
T
e
m
p
e
r
a
t
u
r
e
(4)
(
4
)
°C
°
C
v.t.g
v
.
t
.
g
v.t.g
v
.
t
.
g
v.t.a
v
.
t
.
a
2
2
28
2
8
Water
W
a
t
e
r
content
c
o
n
t
e
n
t
kg/h
k
g
/
h
29
2
9
Pipe
P
i
p
e
diameter
d
i
a
m
e
t
e
r
DN
D
N
84"
8
4
"
2
2
30
3
0
Design
D
e
s
i
g
n
pressure
p
r
e
s
s
u
r
e
bar(g)
b
a
r
(
g
)
9
9
2
2
31
3
1
Design
D
e
s
i
g
n
temperature
t
e
m
p
e
r
a
t
u
r
e
min.
m
i
n
.
/
/
max.
m
a
x
.
°C
°
C
-20
-
2
0
/
/
250
2
5
0
2
2
32
3
2
33
3
3
HOT
H
O
T
WATER
W
A
T
E
R
34
3
4
Minimum
M
i
n
i
m
u
m
available
a
v
a
i
l
a
b
l
e
hot
h
o
t
water
w
a
t
e
r
temperature
t
e
m
p
e
r
a
t
u
r
e
°C
°
C
26.1
2
6
.
1
26.1
2
6
.
1
26.1
2
6
.
1
26.1
2
6
.
1
2
2
35
3
5
36
3
6
ENERGY
E
N
E
R
G
Y
37
3
7
Polytropic
P
o
l
y
t
r
o
p
i
c
efficiency
e
f
f
i
c
i
e
n
c
y
%
%
38
3
8
Thermodynamic
T
h
e
r
m
o
d
y
n
a
m
i
c
power
p
o
w
e
r
kW
k
W
39
3
9
Mechanical
M
e
c
h
a
n
i
c
a
l
losses
l
o
s
s
e
s
(including
(
i
n
c
l
u
d
i
n
g
main
m
a
i
n
oil
o
i
l
pump)
p
u
m
p
)
kW
k
W
40
4
0
Power
P
o
w
e
r
at
a
t
motor
m
o
t
o
r
coupling
c
o
u
p
l
i
n
g
(including
(
i
n
c
l
u
d
i
n
g
losses)
l
o
s
s
e
s
)
kW
k
W
41
4
1
Total
T
o
t
a
l
power
p
o
w
e
r
at
a
t
motor
m
o
t
o
r
terminals
t
e
r
m
i
n
a
l
s
kW
k
W
42
4
2
Motor
M
o
t
o
r
rating
r
a
t
i
n
g
kW
k
W
43
4
3
Surge
S
u
r
g
e
limit
l
i
m
i
t
in
i
n
%
%
of
o
f
flow
f
l
o
w
(p=constant)
(
p
=
c
o
n
s
t
a
n
t
)
%
%
44
4
4
Driver
D
r
i
v
e
r
rotating
r
o
t
a
t
i
n
g
speed
s
p
e
e
d
RPM
R
P
M
45
4
5
Notes:
N
o
t
e
s
:
Nm
N
m
3
3
=
=
m
m
3
3
reduced
r
e
d
u
c
e
d
to
t
o
0°C
0
°
C
and
a
n
d
1.013
1
.
0
1
3
bar
b
a
r
abs.
a
b
s
.
�
�
�
�
46
4
6
(1)
(
1
)
Before
B
e
f
o
r
e
inlet
i
n
l
e
t
flange
f
l
a
n
g
e
(inlet
(
i
n
l
e
t
silencer
s
i
l
e
n
c
e
r
if
i
f
required),
r
e
q
u
i
r
e
d
)
,
no
n
o
inlet
i
n
l
e
t
filter
f
i
l
t
e
r
is
i
s
required.
r
e
q
u
i
r
e
d
.
47
4
7
(2)
(
2
)
Vendor
V
e
n
d
o
r
to
t
o
advise
a
d
v
i
s
e
temperature,
t
e
m
p
e
r
a
t
u
r
e
,
according
a
c
c
o
r
d
i
n
g
to
t
o
design
d
e
s
i
g
n
philosophy
p
h
i
l
o
s
o
p
h
y
page
p
a
g
e
5.
5
.
2
2
48
4
8
(3)
(
3
)
Vendor
V
e
n
d
o
r
to
t
o
advise
a
d
v
i
s
e
on
o
n
the
t
h
e
condensed
c
o
n
d
e
n
s
e
d
fluid
f
l
u
i
d
in
i
n
the
t
h
e
intercooler
i
n
t
e
r
c
o
o
l
e
r
and
a
n
d
%H2O
%
H
2
O
content
c
o
n
t
e
n
t
in
i
n
compressed
c
o
m
p
r
e
s
s
e
d
gas.
g
a
s
.
49
4
9
(4)
(
4
)
Vendor
V
e
n
d
o
r
to
t
o
guarantee
g
u
a
r
a
n
t
e
e
temperature,
t
e
m
p
e
r
a
t
u
r
e
,
according
a
c
c
o
r
d
i
n
g
to
t
o
design
d
e
s
i
g
n
philosophy
p
h
i
l
o
s
o
p
h
y
page
p
a
g
e
5.
5
.
2
2
50
5
0
(5)
(
5
)
Vendor
V
e
n
d
o
r
to
t
o
advise
a
d
v
i
s
e
minimum
m
i
n
i
m
u
m
load
l
o
a
d
of
o
f
the
t
h
e
compressor.
c
o
m
p
r
e
s
s
o
r
.
2
2
(6)
(
6
)
Possibility
P
o
s
s
i
b
i
l
i
t
y
to
t
o
have
h
a
v
e
acid
a
c
i
d
condensates
c
o
n
d
e
n
s
a
t
e
s
in
i
n
intercooler
i
n
t
e
r
c
o
o
l
e
r
during
d
u
r
i
n
g
transitory
t
r
a
n
s
i
t
o
r
y
phases.
p
h
a
s
e
s
.
2
2
Case-Name:
C
a
s
e
-
N
a
m
e
:
:
:
values
v
a
l
u
e
s
to
t
o
be
b
e
guaranteed
g
u
a
r
a
n
t
e
e
d
by
b
y
vendor
v
e
n
d
o
r
with
w
i
t
h
the
t
h
e
following
f
o
l
l
o
w
i
n
g
tolerances
t
o
l
e
r
a
n
c
e
s
:
:
Pressure
P
r
e
s
s
u
r
e
(-
(
-
0
0
%)
%
)
;
;
Power
P
o
w
e
r
construction
c
o
n
s
t
r
u
c
t
i
o
n
tolerances
t
o
l
e
r
a
n
c
e
s
(+
(
+
0
0
%)
%
)
;
;
Power
P
o
w
e
r
measurement
m
e
a
s
u
r
e
m
e
n
t
tolerances
t
o
l
e
r
a
n
c
e
s
(<
(
<
1.5
1
.
5
%,
%
,
advise
a
d
v
i
s
e
if
i
f
different)
d
i
f
f
e
r
e
n
t
)
;
;
Discharged
D
i
s
c
h
a
r
g
e
d
flow
f
l
o
w
(-
(
-
0
0
%)
%
)
;
;
Temperature
T
e
m
p
e
r
a
t
u
r
e
(+
(
+
1°C)
1
°
C
)
;
;
Water
W
a
t
e
r
flow
f
l
o
w
(+
(
+
5
5
%)
%
)
;
;
Leakage
L
e
a
k
a
g
e
flowrate
f
l
o
w
r
a
t
e
of
o
f
process
p
r
o
c
e
s
s
gas
g
a
s
(+
(
+
0
0
%)
%
)
0Project
0
P
r
o
j
e
c
t
Project
P
r
o
j
e
c
t
Name
N
a
m
e
No.Document
N
o
.
D
o
c
u
m
e
n
t
No.
N
o
.
ACCSION
A
C
C
S
I
O
N
53573
5
3
5
7
3
53573-62-01-PR-013712
5
3
5
7
3
-
6
2
-
0
1
-
P
R
-
0
1
3
7
1
2
N/A
N
/
A
:
:
values
v
a
l
u
e
s
to
t
o
be
b
e
advised
a
d
v
i
s
e
d
by
b
y
vendor.
v
e
n
d
o
r
.
Process
P
r
o
c
e
s
s
Process
P
r
o
c
e
s
s
Data
D
a
t
a
Sheet
S
h
e
e
t
Compressor
C
o
m
p
r
e
s
s
o
r
Printed
P
r
i
n
t
e
d
by
b
y
/
/
date
d
a
t
e
/
/
time:
t
i
m
e
:
client-logo.bmp
c
l
i
e
n
t
-
l
o
g
o
.
b
m
p
Line
L
i
n
e
revised
r
e
v
i
s
e
d
under
u
n
d
e
r
Rev.
R
e
v
.
No.
N
o
.
Sheet
S
h
e
e
t
/
/
of
o
f
3
3
/
/
7
7
Revision
R
e
v
i
s
i
o
n
2
2
RNETW
R
N
E
T
W
/
/
05/06/26
0
5
/
0
6
/
2
6
/
/
16:22
1
6
:
2
2
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e
other
o
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than
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h
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n
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h
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t
for
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o
r
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return
r
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r
n
on
o
n
demand.
d
e
m
a
n
d
.
●INTERNAL
●
I
N
T
E
R
N
A
L
Process
P
r
o
c
e
s
s
Item
I
t
e
m
Specifications
S
p
e
c
i
f
i
c
a
t
i
o
n
s
&
&
Data
D
a
t
a
Sheets
S
h
e
e
t
s
Process
P
r
o
c
e
s
s
Data
D
a
t
a
Sheet
S
h
e
e
t
Compressor
C
o
m
p
r
e
s
s
o
r
01
0
1
Item
I
t
e
m
Number
N
u
m
b
e
r
02
0
2
621001C12
6
2
1
0
0
1
C
1
2
03
0
3
Designation
D
e
s
i
g
n
a
t
i
o
n
PROCESS
P
R
O
C
E
S
S
DATA
D
A
T
A
-
-
WET
W
E
T
FEED
F
E
E
D
GAS
G
A
S
COMPRESSOR
C
O
M
P
R
E
S
S
O
R
04
0
4
05
0
5
06
0
6
CASE
C
A
S
E
07
0
7
08
0
8
09
0
9
HOT
H
O
T
WATER
W
A
T
E
R
10
1
0
ME-
M
E
-
Glycol
G
l
y
c
o
l
content
c
o
n
t
e
n
t
in
i
n
hot
h
o
t
water
w
a
t
e
r
%
%
vol
v
o
l
11
1
1
Hot
H
o
t
water
w
a
t
e
r
flowrate
f
l
o
w
r
a
t
e
m
m
3
3
/h
/
h
12
1
2
Hot
H
o
t
water
w
a
t
e
r
intercooler
i
n
t
e
r
c
o
o
l
e
r
outlet
o
u
t
l
e
t
temperature
t
e
m
p
e
r
a
t
u
r
e
°C
°
C
RATED
R
A
T
E
D
DESIGN
D
E
S
I
G
N
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
NOMINAL
N
O
M
I
N
A
L
WINTER
W
I
N
T
E
R
0
0
v.t.a
v
.
t
.
a
v.t.a
v
.
t
.
a
Gas
G
a
s
T
T
in
i
n
-
-
6°C
6
°
C
(8)
(
8
)
NOMINAL
N
O
M
I
N
A
L
SUMMER
S
U
M
M
E
R
START
S
T
A
R
T
UP
U
P
13
1
3
Water
W
a
t
e
r
fouling
f
o
u
l
i
n
g
factor
f
a
c
t
o
r
m
m
2
2
h°C/kcal
h
°
C
/
k
c
a
l
0.0001
0
.
0
0
0
1
2
2
14
1
4
Water
W
a
t
e
r
inlet
i
n
l
e
t
pressure
p
r
e
s
s
u
r
e
bar(a)
b
a
r
(
a
)
19.5
1
9
.
5
2
2
15
1
5
Allowable
A
l
l
o
w
a
b
l
e
water
w
a
t
e
r
pressure
p
r
e
s
s
u
r
e
drop
d
r
o
p
(skid)
(
s
k
i
d
)
mbar
m
b
a
r
2
2
500
5
0
0
2
2
16
1
6
Design
D
e
s
i
g
n
pressure
p
r
e
s
s
u
r
e
barg
b
a
r
g
25.0
2
5
.
0
17
1
7
Design
D
e
s
i
g
n
temperature
t
e
m
p
e
r
a
t
u
r
e
min.
m
i
n
.
/
/
max.
m
a
x
.
°C
°
C
-20
-
2
0
/
/
230
2
3
0
18
1
8
19
1
9
20
2
0
COOLING
C
O
O
L
I
N
G
WATER
W
A
T
E
R
(for
(
f
o
r
auxiliary
a
u
x
i
l
i
a
r
y
equipment)
e
q
u
i
p
m
e
n
t
)
21
2
1
ME-
M
E
-
Glycol
G
l
y
c
o
l
content
c
o
n
t
e
n
t
in
i
n
cooling
c
o
o
l
i
n
g
water
w
a
t
e
r
%
%
vol
v
o
l
0
0
22
2
2
Cooling
C
o
o
l
i
n
g
water
w
a
t
e
r
temperature
t
e
m
p
e
r
a
t
u
r
e
-
-
process
p
r
o
c
e
s
s
design
d
e
s
i
g
n
°C
°
C
23.1
2
3
.
1
13.4
1
3
.
4
18.7
1
8
.
7
23.1
2
3
.
1
2
2
23
2
3
Cooling
C
o
o
l
i
n
g
water
w
a
t
e
r
supply
s
u
p
p
l
y
pressure
p
r
e
s
s
u
r
e
bar
b
a
r
(a)
(
a
)
4.0
4
.
0
24
2
4
Temperature
T
e
m
p
e
r
a
t
u
r
e
elevation
e
l
e
v
a
t
i
o
n
in
i
n
equipment
e
q
u
i
p
m
e
n
t
(skid)
(
s
k
i
d
)
°C
°
C
15.0
1
5
.
0
25
2
5
Allowable
A
l
l
o
w
a
b
l
e
water
w
a
t
e
r
pressure
p
r
e
s
s
u
r
e
drop
d
r
o
p
(skid)
(
s
k
i
d
)
mbar
m
b
a
r
1
1
000
0
0
0
26
2
6
27
2
7
28
2
8
UTILITIES
U
T
I
L
I
T
I
E
S
29
2
9
Seal
S
e
a
l
gas
g
a
s
nature
n
a
t
u
r
e
(9)
(
9
)
30
3
0
Seal
S
e
a
l
gas
g
a
s
flowrate
f
l
o
w
r
a
t
e
(standstill
(
s
t
a
n
d
s
t
i
l
l
/
/
normal
n
o
r
m
a
l
operation)
o
p
e
r
a
t
i
o
n
)
Nm
N
m
3
3
/h
/
h
31
3
1
Seal
S
e
a
l
gas
g
a
s
leakage
l
e
a
k
a
g
e
into
i
n
t
o
process
p
r
o
c
e
s
s
section
s
e
c
t
i
o
n
(overall)
(
o
v
e
r
a
l
l
)
Nm
N
m
3
3
/h
/
h
32
3
2
Seal
S
e
a
l
gas
g
a
s
leakage
l
e
a
k
a
g
e
to
t
o
atmosphere
a
t
m
o
s
p
h
e
r
e
(overall)
(
o
v
e
r
a
l
l
)
Nm
N
m
3
3
/h
/
h
33
3
3
Minimum
M
i
n
i
m
u
m
seal
s
e
a
l
gas
g
a
s
pressure
p
r
e
s
s
u
r
e
bara
b
a
r
a
34
3
4
Instrument
I
n
s
t
r
u
m
e
n
t
air
a
i
r
flowrate
f
l
o
w
r
a
t
e
Nm
N
m
3
3
/h
/
h
35
3
5
Frequency
F
r
e
q
u
e
n
c
y
Hz
H
z
50.0
5
0
.
0
36
3
6
37
3
7
38
3
8
Notes:
N
o
t
e
s
:
Nm
N
m
3
3
=
=
m
m
3
3
reduced
r
e
d
u
c
e
d
to
t
o
0°C
0
°
C
and
a
n
d
1.013
1
.
0
1
3
bar
b
a
r
abs.
a
b
s
.
39
3
9
40
4
0
41
4
1
(8)
(
8
)
See
S
e
e
page
p
a
g
e
5
5
for
f
o
r
design
d
e
s
i
g
n
philosophy.
p
h
i
l
o
s
o
p
h
y
.
Minimum
M
i
n
i
m
u
m
hot
h
o
t
water
w
a
t
e
r
temperature
t
e
m
p
e
r
a
t
u
r
e
is
i
s
118°C.
1
1
8
°
C
.
2
2
42
4
2
(9)
(
9
)
Please
P
l
e
a
s
e
refer
r
e
f
e
r
to
t
o
Technical
T
e
c
h
n
i
c
a
l
Requisition
R
e
q
u
i
s
i
t
i
o
n
Summary.
S
u
m
m
a
r
y
.
43
4
3
44
4
4
:
:
values
v
a
l
u
e
s
to
t
o
be
b
e
advised
a
d
v
i
s
e
d
by
b
y
vendor.
v
e
n
d
o
r
.
45
4
5
46
4
6
:
:
values
v
a
l
u
e
s
to
t
o
be
b
e
guaranteed
g
u
a
r
a
n
t
e
e
d
by
b
y
vendor
v
e
n
d
o
r
with
w
i
t
h
the
t
h
e
following
f
o
l
l
o
w
i
n
g
tolerances
t
o
l
e
r
a
n
c
e
s
:
:
Pressure
P
r
e
s
s
u
r
e
(-
(
-
0
0
%)
%
)
;
;
Power
P
o
w
e
r
construction
c
o
n
s
t
r
u
c
t
i
o
n
tolerances
t
o
l
e
r
a
n
c
e
s
(+
(
+
0
0
%)
%
)
;
;
47
4
7
Power
P
o
w
e
r
measurement
m
e
a
s
u
r
e
m
e
n
t
tolerances
t
o
l
e
r
a
n
c
e
s
(<
(
<
1.5
1
.
5
%,
%
,
advise
a
d
v
i
s
e
if
i
f
different)
d
i
f
f
e
r
e
n
t
)
;
;
Discharged
D
i
s
c
h
a
r
g
e
d
flow
f
l
o
w
(-
(
-
0
0
%)
%
)
;
;
Temperature
T
e
m
p
e
r
a
t
u
r
e
(+
(
+
1°C)
1
°
C
)
;
;
48
4
8
Water
W
a
t
e
r
flow
f
l
o
w
(+
(
+
5
5
%)
%
)
;
;
Leakage
L
e
a
k
a
g
e
flowrate
f
l
o
w
r
a
t
e
of
o
f
process
p
r
o
c
e
s
s
gas
g
a
s
(+
(
+
0
0
%)
%
)
49
4
9
v.t.a
v
.
t
.
a
2
2
Derived
D
e
r
i
v
e
d
from
f
r
o
m
G-TPL-13-0-1,
G
-
T
P
L
-
1
3
-
0
-
1
,
Rev.
R
e
v
.
1,
1
,
issued
i
s
s
u
e
d
26-Jun-18
2
6
-
J
u
n
-
1
8
Rev.
R
e
v
.
0
0
AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR
A
L
_
C
R
Y
O
_
P
R
O
C
E
S
S
_
D
S
_
T
E
M
P
L
A
T
E
_
C
O
M
P
R
E
S
S
O
R
Line
L
i
n
e
revised
r
e
v
i
s
e
d
under
u
n
d
e
r
Rev.
R
e
v
.
No.
N
o
.
Project
P
r
o
j
e
c
t
Name
N
a
m
e
Project
P
r
o
j
e
c
t
No.
N
o
.
Document
D
o
c
u
m
e
n
t
No.
N
o
.
Sheet
S
h
e
e
t
/
/
of
o
f
Revision
R
e
v
i
s
i
o
n
ACCSION
A
C
C
S
I
O
N
53573
5
3
5
7
3
53573-62-01-PR-013712
5
3
5
7
3
-
6
2
-
0
1
-
P
R
-
0
1
3
7
1
2
4
4
/
/
7
7
2
2
Case-Name:
C
a
s
e
-
N
a
m
e
:
N/A
N
/
A
Printed
P
r
i
n
t
e
d
by
b
y
/
/
date
d
a
t
e
/
/
time:
t
i
m
e
:
RNETW
R
N
E
T
W
/
/
05/06/26
0
5
/
0
6
/
2
6
/
/
16:22
1
6
:
2
2
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Air
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i
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o
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i
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i
a
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o
r
m
a
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i
o
n
This
T
h
i
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print
p
r
i
n
t
is
i
s
the
t
h
e
property
p
r
o
p
e
r
t
y
of
o
f
L’Air
L
’
A
i
r
Liquide
L
i
q
u
i
d
e
S.A.
S
.
A
.
or
o
r
its
i
t
s
(direct
(
d
i
r
e
c
t
and
a
n
d
indirect)
i
n
d
i
r
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o
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h
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d
●INTERNAL
●
I
N
T
E
R
N
A
L
Derived
D
e
r
i
v
e
d
from
f
r
o
m
G-TPL-13-0-1,
G
-
T
P
L
-
1
3
-
0
-
1
,
Rev.
R
e
v
.
1,
1
,
issued
i
s
s
u
e
d
26-Jun-18
2
6
-
J
u
n
-
1
8
party,
p
a
r
t
y
,
reproduced,
r
e
p
r
o
d
u
c
e
d
,
copied,
c
o
p
i
e
d
,
lent,
l
e
n
t
,
or
o
r
disposed
d
i
s
p
o
s
e
d
of,
o
f
,
directly
d
i
r
e
c
t
l
y
or
o
r
indirectly,
i
n
d
i
r
e
c
t
l
y
,
nor
n
o
r
used
u
s
e
d
for
f
o
r
any
a
n
y
purpose
p
u
r
p
o
s
e
other
o
t
h
e
r
than
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a
n
that
t
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a
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for
f
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h
it
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t
is
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s
expressly
e
x
p
r
e
s
s
l
y
Rev.
R
e
v
.
furnished.
f
u
r
n
i
s
h
e
d
.
This
T
h
i
s
print
p
r
i
n
t
is
i
s
lent
l
e
n
t
subject
s
u
b
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to
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o
return
r
e
t
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r
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on
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.
AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR
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PROCESS
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D
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COMPRESSOR
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Number
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D
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S
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PHILOSOPHY
P
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08
0
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09
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Step
S
t
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p
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�
Compander
C
o
m
p
a
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d
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r
-
-
Expander
E
x
p
a
n
d
e
r
side
s
i
d
e
10
1
0
Determine
D
e
t
e
r
m
i
n
e
the
t
h
e
temperature
t
e
m
p
e
r
a
t
u
r
e
needed
n
e
e
d
e
d
at
a
t
the
t
h
e
inlet
i
n
l
e
t
of
o
f
the
t
h
e
expander
e
x
p
a
n
d
e
r
(=
(
=
a1)
a
1
)
to
t
o
reach
r
e
a
c
h
2°C
2
°
C
after
a
f
t
e
r
the
t
h
e
expansion.
e
x
p
a
n
s
i
o
n
.
Use
U
s
e
a1
a
1
in
i
n
the
t
h
e
following
f
o
l
l
o
w
i
n
g
formula
f
o
r
m
u
l
a
to
t
o
determine
d
e
t
e
r
m
i
n
e
11
1
1
the
t
h
e
temperature
t
e
m
p
e
r
a
t
u
r
e
needed
n
e
e
d
e
d
at
a
t
the
t
h
e
outlet
o
u
t
l
e
t
of
o
f
the
t
h
e
Flue
F
l
u
e
Gas
G
a
s
Compressor
C
o
m
p
r
e
s
s
o
r
(=
(
=
z1)
z
1
)
:
:
12
1
2
z1
z
1
=
=
a1
a
1
+
+
45°C
4
5
°
C
and
a
n
d
minimum
m
i
n
i
m
u
m
z1
z
1
value
v
a
l
u
e
should
s
h
o
u
l
d
be
b
e
181°C
1
8
1
°
C
13
1
3
14
1
4
STEP
S
T
E
P
1
1
15
1
5
Variables
V
a
r
i
a
b
l
e
s
Fixed
F
i
x
e
d
values
v
a
l
u
e
s
Calculated
C
a
l
c
u
l
a
t
e
d
values
v
a
l
u
e
s
16
1
6
a1
a
1
2°C
2
°
C
after
a
f
t
e
r
expansion
e
x
p
a
n
s
i
o
n
z1
z
1
17
1
7
18
1
8
Step
S
t
e
p
2
2
�
Flue
F
l
u
e
Gas
G
a
s
Compressor
C
o
m
p
r
e
s
s
o
r
-
-
Nominal
N
o
m
i
n
a
l
Winter
W
i
n
t
e
r
Case
C
a
s
e
19
1
9
On
O
n
this
t
h
i
s
case,
c
a
s
e
,
determine
d
e
t
e
r
m
i
n
e
the
t
h
e
optimum
o
p
t
i
m
u
m
pressure
p
r
e
s
s
u
r
e
at
a
t
the
t
h
e
outlet
o
u
t
l
e
t
of
o
f
the
t
h
e
first
f
i
r
s
t
stage.
s
t
a
g
e
.
Make
M
a
k
e
sure
s
u
r
e
that
t
h
a
t
the
t
h
e
gas
g
a
s
temperature
t
e
m
p
e
r
a
t
u
r
e
is
i
s
high
h
i
g
h
enough
e
n
o
u
g
h
so
s
o
that
t
h
a
t
the
t
h
e
hot
h
o
t
20
2
0
water
w
a
t
e
r
temperature
t
e
m
p
e
r
a
t
u
r
e
is
i
s
not
n
o
t
lower
l
o
w
e
r
than
t
h
a
n
118°C.
1
1
8
°
C
.
Use
U
s
e
formula
f
o
r
m
u
l
a
Tw_out
T
w
_
o
u
t
=
=
Tg_in
T
g
_
i
n
-
-
6°C
6
°
C
:
:
21
2
1
STEP
S
T
E
P
2
2
22
2
2
Variables
V
a
r
i
a
b
l
e
s
Fixed
F
i
x
e
d
values
v
a
l
u
e
s
Calculated
C
a
l
c
u
l
a
t
e
d
values
v
a
l
u
e
s
23
2
3
Intermediate
I
n
t
e
r
m
e
d
i
a
t
e
P
P
Tg_in
T
g
_
i
n
Tw_out
T
w
_
o
u
t
24
2
4
25
2
5
26
2
6
27
2
7
28
2
8
29
2
9
30
3
0
31
3
1
32
3
2
33
3
3
34
3
4
35
3
5
36
3
6
37
3
7
38
3
8
39
3
9
40
4
0
41
4
1
42
4
2
43
4
3
44
4
4
45
4
5
46
4
6
47
4
7
48
4
8
49
4
9
50
5
0
Qin=
Q
i
n
=
552
5
5
2
936
9
3
6
Nm3/h
N
m
3
/
h
or
o
r
767
7
6
7
768
7
6
8
kg/h
k
g
/
h
Tsuction
T
s
u
c
t
i
o
n
=
=
35°C
3
5
°
C
Still
S
t
i
l
l
on
o
n
the
t
h
e
Nominal
N
o
m
i
n
a
l
Winter
W
i
n
t
e
r
case,
c
a
s
e
,
work
w
o
r
k
on
o
n
the
t
h
e
second
s
e
c
o
n
d
section
s
e
c
t
i
o
n
of
o
f
the
t
h
e
compressor
c
o
m
p
r
e
s
s
o
r
to
t
o
determine
d
e
t
e
r
m
i
n
e
which
w
h
i
c
h
intercooler
i
n
t
e
r
c
o
o
l
e
r
gas
g
a
s
outlet
o
u
t
l
e
t
temperature
t
e
m
p
e
r
a
t
u
r
e
(=y2)
(
=
y
2
)
allows
a
l
l
o
w
s
to
t
o
reach
r
e
a
c
h
calculated
c
a
l
c
u
l
a
t
e
d
specification
s
p
e
c
i
f
i
c
a
t
i
o
n
on
o
n
discharge
d
i
s
c
h
a
r
g
e
temperature
t
e
m
p
e
r
a
t
u
r
e
(=z1)
(
=
z
1
)
:
:
Qin=
Q
i
n
=
552
5
5
2
936
9
3
6
Nm3/h
N
m
3
/
h
or
o
r
767
7
6
7
768
7
6
8
kg/h
k
g
/
h
Tsuction
T
s
u
c
t
i
o
n
=
=
35°C
3
5
°
C
STEP
S
T
E
P
3
3
Variables
V
a
r
i
a
b
l
e
s
Fixed
F
i
x
e
d
values
v
a
l
u
e
s
Calculated
C
a
l
c
u
l
a
t
e
d
values
v
a
l
u
e
s
y2
y
2
z1
z
1
-
-
On
O
n
the
t
h
e
rated
r
a
t
e
d
case,
c
a
s
e
,
reinject
r
e
i
n
j
e
c
t
the
t
h
e
temperature
t
e
m
p
e
r
a
t
u
r
e
y2
y
2
determined
d
e
t
e
r
m
i
n
e
d
in
i
n
step
s
t
e
p
2
2
as
a
s
the
t
h
e
gas
g
a
s
outlet
o
u
t
l
e
t
temperature
t
e
m
p
e
r
a
t
u
r
e
and
a
n
d
design
d
e
s
i
g
n
the
t
h
e
intercooler
i
n
t
e
r
c
o
o
l
e
r
on
o
n
the
t
h
e
Rated
R
a
t
e
d
case
c
a
s
e
conditions.
c
o
n
d
i
t
i
o
n
s
.
Use
U
s
e
an
a
n
approach
a
p
p
r
o
a
c
h
of
o
f
6°C
6
°
C
between
b
e
t
w
e
e
n
gas
g
a
s
inlet
i
n
l
e
t
temperature
t
e
m
p
e
r
a
t
u
r
e
and
a
n
d
water
w
a
t
e
r
outlet
o
u
t
l
e
t
temperature
t
e
m
p
e
r
a
t
u
r
e
:
:
Qin=
Q
i
n
=
601
6
0
1
413
4
1
3
Nm3/h
N
m
3
/
h
or
o
r
835
8
3
5
595
5
9
5
kg/h
k
g
/
h
Tsuction
T
s
u
c
t
i
o
n
=
=
35°C
3
5
°
C
Stage
S
t
a
g
e
1
1
Stage
S
t
a
g
e
1
1
Stages
S
t
a
g
e
s
2
2
&3
&
3
Tdischarge
T
d
i
s
c
h
a
r
g
e
=
=
z1°C
z
1
°
C
STEP
S
T
E
P
4
4
Variables
V
a
r
i
a
b
l
e
s
Fixed
F
i
x
e
d
values
v
a
l
u
e
s
Calculated
C
a
l
c
u
l
a
t
e
d
values
v
a
l
u
e
s
Hot
H
o
t
water
w
a
t
e
r
flow
f
l
o
w
y2
y
2
;
;
Tw_in
T
w
_
i
n
x1
x
1
;
;
intercooler
i
n
t
e
r
c
o
o
l
e
r
UA
U
A
;
;
Tw_out
T
w
_
o
u
t
;
;
Tdischarge
T
d
i
s
c
h
a
r
g
e
Stage
S
t
a
g
e
1
1
Tg_in
T
g
_
i
n
=
=
x2
x
2
Tg_out
T
g
_
o
u
t
=
=
y2
y
2
Tw_out
T
w
_
o
u
t
=
=
x2-6°C
x
2
-
6
°
C
Tg_in
T
g
_
i
n
=
=
x2
x
2
Tg_out
T
g
_
o
u
t
=
=
y2
y
2
Tw_out
T
w
_
o
u
t
=
=
x2-6°C
x
2
-
6
°
C
Tw_in
T
w
_
i
n
=
=
26.1°C
2
6
.
1
°
C
Tw_in
T
w
_
i
n
=
=
26.1°C
2
6
.
1
°
C
UA
U
A
installed
i
n
s
t
a
l
l
e
d
=
=
Rated
R
a
t
e
d
Design
D
e
s
i
g
n
Tg_in
T
g
_
i
n
=
=
x1
x
1
Tg_out
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g
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o
u
t
=
=
y2
y
2
Tw_out
T
w
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o
u
t
=
=
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x
l
-
6
°
C
Tw_in
T
w
_
i
n
=
=
26.1°C
2
6
.
1
°
C
Stages
S
t
a
g
e
s
2
2
&3
&
3
Stages
S
t
a
g
e
s
2
2
&3
&
3
Tdischarge
T
d
i
s
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e
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1
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Tdischarge
T
d
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c
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°
C
Line
L
i
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revised
r
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v
i
s
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under
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e
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Rev.
R
e
v
.
No.
N
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.
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0
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c
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NameProject
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No.
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Document
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Sheet
S
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t
/
/
of
o
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Revision
R
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v
i
s
i
o
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ACCSION
A
C
C
S
I
O
N
53573
5
3
5
7
3
53573-62-01-PR-013712
5
3
5
7
3
-
6
2
-
0
1
-
P
R
-
0
1
3
7
1
2
5
5
/
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7
7
2
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Case-Name:
C
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:
N/A
N
/
A
Printed
P
r
i
n
t
e
d
by
b
y
/
/
date
d
a
t
e
/
/
time:
t
i
m
e
:
RNETW
R
N
E
T
W
/
/
05/06/26
0
5
/
0
6
/
2
6
/
/
16:22
1
6
:
2
2
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Air
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Liquide
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Confidential
C
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f
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Information
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This
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print
p
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the
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property
p
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p
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of
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L’Air
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A
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c
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a
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information.
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Copyright
C
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p
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and
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all
a
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other
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are
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Derived
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from
f
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G-TPL-13-0-1,
G
-
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P
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-
1
3
-
0
-
1
,
Rev.
R
e
v
.
1,
1
,
issued
i
s
s
u
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26-Jun-18
2
6
-
J
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1
8
party,
p
a
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c
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AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR
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Data
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values
v
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Number
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Designation
D
e
s
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n
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PROCESS
P
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DATA
D
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WET
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FEED
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COMPRESSOR
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Number
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and
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the
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11
1
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previous
p
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outlet
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t
temperature
t
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m
p
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r
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y2
y
2
:
:
13
1
3
14
1
4
15
1
5
16
1
6
17
1
7
18
1
8
19
1
9
20
2
0
21
2
1
22
2
2
23
2
3
24
2
4
25
2
5
26
2
6
27
2
7
28
2
8
29
2
9
30
3
0
31
3
1
32
3
2
33
3
3
34
3
4
35
3
5
36
3
6
37
3
7
38
3
8
39
3
9
40
4
0
41
4
1
42
4
2
43
4
3
44
4
4
45
4
5
46
4
6
47
4
7
48
4
8
49
4
9
50
5
0
Case-Name:
C
a
s
e
-
N
a
m
e
:
N/A
N
/
A
Qin=
Q
i
n
=
552
5
5
2
936
9
3
6
Nm3/h
N
m
3
/
h
or
o
r
767
7
6
7
768
7
6
8
kg/h
k
g
/
h
Tsuction
T
s
u
c
t
i
o
n
=
=
35°C
3
5
°
C
Variables
V
a
r
i
a
b
l
e
s
Hot
H
o
t
water
w
a
t
e
r
flow
f
l
o
w
Stage
S
t
a
g
e
1
1
UA
U
A
installed
i
n
s
t
a
l
l
e
d
=
=
Rated
R
a
t
e
d
Design
D
e
s
i
g
n
Tg_in
T
g
_
i
n
=
=
x2
x
2
Tg_out
T
g
_
o
u
t
=
=
y2
y
2
Tw_out
T
w
_
o
u
t
=
=
x2-6°C
x
2
-
6
°
C
Tw_in
T
w
_
i
n
=
=
26.1°C
2
6
.
1
°
C
Stages
S
t
a
g
e
s
2
2
&3
&
3
Tdischarge
T
d
i
s
c
h
a
r
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e
=
=
z1
z
1
Line
L
i
n
e
revised
r
e
v
i
s
e
d
under
u
n
d
e
r
Rev.
R
e
v
.
No.
N
o
.
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0
P
r
o
j
e
c
t
NameProject
N
a
m
e
P
r
o
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e
c
t
No.
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o
.
Document
D
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c
u
m
e
n
t
No.
N
o
.
Sheet
S
h
e
e
t
/
/
of
o
f
Revision
R
e
v
i
s
i
o
n
ACCSION
A
C
C
S
I
O
N
53573
5
3
5
7
3
53573-62-01-PR-013712
5
3
5
7
3
-
6
2
-
0
1
-
P
R
-
0
1
3
7
1
2
6
6
/
/
7
7
2
2
Printed
P
r
i
n
t
e
d
by
b
y
/
/
date
d
a
t
e
/
/
time:
t
i
m
e
:
RNETW
R
N
E
T
W
/
/
05/06/26
0
5
/
0
6
/
2
6
/
/
16:22
1
6
:
2
2
granularity=word tetml={elements={line} glyphdetails={all}} contentanalysis={punctuationbreaks=false dehyphenate=false shadowdetect=false} layoutanalysis={tabledetect=0 layoutdetect=3} structureanalysis={list=true}
Ammonia
A
m
m
o
n
i
a
(NH3)
(
N
H
3
)
Formaldehyde
F
o
r
m
a
l
d
e
h
y
d
e
Acetaldehyde
A
c
e
t
a
l
d
e
h
y
d
e
Others
O
t
h
e
r
s
Total
T
o
t
a
l
Mercury
M
e
r
c
u
r
y
(Hg)
(
H
g
)
PCDD
P
C
D
D
/
/
PCDF
P
C
D
F
HAP
H
A
P
-
-
EPA
E
P
A
BTEX
B
T
E
X
Molar
M
o
l
a
r
Heat
H
e
a
t
Capacity
C
a
p
a
c
i
t
y
(10)
(
1
0
)
kcal/Nm3/°C
k
c
a
l
/
N
m
3
/
°
C
Viscosity
V
i
s
c
o
s
i
t
y
(10)
(
1
0
)
kg/m/h
k
g
/
m
/
h
Notes
N
o
t
e
s
:
:
(10)
(
1
0
)
Physical
P
h
y
s
i
c
a
l
properties
p
r
o
p
e
r
t
i
e
s
at
a
t
suction
s
u
c
t
i
o
n
Dust
D
u
s
t
content
c
o
n
t
e
n
t
µg/Nm
µ
g
/
N
m
3
3
Acid
A
c
i
d
Process
P
r
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c
e
s
s
Condensates
C
o
n
d
e
n
s
a
t
e
s
Line
L
i
n
e
revised
r
e
v
i
s
e
d
under
u
n
d
e
r
Rev.
R
e
v
.
No.
N
o
.
2
2
Nm
N
m
3
3
=
=
m
m
3
3
reduced
r
e
d
u
c
e
d
to
t
o
0°C
0
°
C
and
a
n
d
1.013
1
.
0
1
3
bar
b
a
r
abs.
a
b
s
.
�
�
�
�
μg/Nm3
μ
g
/
N
m
3
mg/Nm3
m
g
/
N
m
3
31.12
3
1
.
1
2
NOMINAL
N
O
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WINTER
W
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T
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N
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SUMMER
S
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Composition
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b
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Oxygen
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%mol
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l
Argon
A
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A
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N
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23
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17.2
1
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2
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.
3
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m
32
3
2
0.1
0
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1
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3
3
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0.313
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.
3
3
3
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7
.
1
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p
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m
Methane
M
e
t
h
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(
C
H
4
4
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)
46
4
6
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9
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5
0
47
4
7
48
4
8
43
4
3
0.065
0
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0
6
5
0.065
0
.
0
6
5
37
3
7
38
3
8
Dust
D
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10
1
0
35
3
5
/
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N/A
N
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A
Printed
P
r
i
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t
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b
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/
/
date
d
a
t
e
/
/
time:
t
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:
RNETW
R
N
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T
W
/
/
05/06/26
0
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0
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2
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of
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Revision
R
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Please
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Case-Name:
C
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N
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:
16:22
1
6
:
2
2
Rev.
R
e
v
.
53573
5
3
5
7
3
53573-62-01-PR-013712
5
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ACCSION
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No.Document
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No.
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AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR
A
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from
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G-TPL-13-0-1,
G
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,
Rev.
R
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v
.
1,
1
,
issued
i
s
s
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26-Jun-18
2
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Project
P
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Name
N
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31.31
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0
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28.76
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Molecular
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r
Weight
W
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(10)
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●INTERNAL
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N
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21
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Mass
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0
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2
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FLUID
F
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Driver
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Electrical
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68.31
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Number
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Confidential
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Information
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This
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print
p
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0.00
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0.69
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0.50
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0.20
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0.60