ARNOLD, K (1999) Design of Gas-Handling Systems and Facilities (2nd ed ) Episode 2 Part 6 docx
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 6 docx
... 388 —
1 .22
339
1. 52
366
1. 82
389 — —
1 .23
340
1.53
367
1.83
389 —
—•
1 .24
341
1.54
368
1.84
390
—
1 .25
3 42
1.55
369
1.85
391 — —
1 . 26
343
1. 56
369
1. 86
391
—
1 .27
344
... 13-3
Standard
Orifice
Areas
and
Designations
Orifice
D
E
F
G
H
J
K
L
M
N
P
Q
R
T
Area
in.
2
0.110
0.1 96
0.307
0.503
0.785
1 .28 7
1.838
2. 853
3 .60
4.34
6....
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx
... 140°F
Reid
Vapor Pressure
34
30
26
22
18
14
10
25
!
Grade 34 -25
Grade 30 -25
Grade 26 -25
Grade 22 -25
Grade
18 -25
Grade 14 -25
40
i
Grade
34-40
Grade
30-40
Grade 26 -40
Grade
22 -40
Grade 18-40
Grade 14-40
55
i
Grade ... Typically, high-speed compressors
run at a
speed
of 900 to
J
20 0
rpm
and
slow-speed
units
at
speeds
of 20 0 to 60 0
rpm.
24 0...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 7 docx
... Figure
14 -2.
Hazard
free
for
production
facility.
(Source:
API
RP14 .)
Figure
14*4, Continued.
410
Design
of
GAS-HANDLING
Systems
and
Facilities
(text
continued
from
page 40 6)
nal
... 14.5.
{figure
continued
on
pugf)
3 96
Design
of
GAS-HANDLING
Systems
and
Facilities
detectors
and
manual shutdown stations
to
provide
adequate
warning...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 8 docx
... (Courtesy
of
Jenkins
Bros .)
430
Design
of
GAS-HANDLING
Systems
and
Facilities
Table
15 -2
(Continued)
Example
Specifications
of
Pipe,
Valves,
and
Fittings
Couplings
1
-in.
and
smaller
... ofXomox
Corp .)
4 26
Design
of
GAS-HANDLING
Systems
and
Facilities
5.
Welding certification
and
inspection requirements.
6,
Design details
(if...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 13 docx
... positive-displacement,
25 5
bearings,
29 6 -29 8
reciprocating,
3,
25 5 - 26 4 ,28 6- 3 26
booster,
25 4, 27 6,
28 6
high-speed,
25 8 -25 9
capacity
control devices,
3 02
low-speed,
25 9 - 26 4
casinghead
gas,
25 4
process ... considerations,
27 6 -28 0
centrifugal,
3,
26 7 -27 0,
28 6
rod, 29 4,
310-311
centr
i
fugal
proces
s
considerations,...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx
... 9,050
2
1
A
0.750 10, 720 12, 490
2
1
A
0.875 12, 530 14 ,60 0
3Std
0 .21 6
2, 260
—
3XS
0.300 3 ,20 0
—
3XXS
0 .60 0 6, 820 7,940
4Std
0 .23 7
1, 920
—
4XS
0.337 2, 770
—
4XXS
0 .67 4 5, 860 6, 830
6Std
... 2O-0''
8 -2- XH
8-y'XXH
8 -2& quot;XH
8 -2& quot;XXH
TO-r'XH
io-r'xxM
6- 3"XH
6- 3"XXH
2- 2"XH
12- r'XXH
WXH
8.3...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps
... Gas
Vapor
Recovery
Flow
Rate
MMscfd
100
10
5
20
100
2
2
4
0.1
1.0
2. 0
R
2. 0
2. 0
2. 7
2, 7
2. 7
2. 0
2. 0
2. 0
4.0
3.0
3.0
n
1
!
3
3
.3
1
2
2
1
2
2
Approx.
bhp
4,400
440
980
3, 920
19 ,6 02
88
190
380
9
143
28 6
Most
Likely
Centrifugal
High
Speed
High ... service.
26 2
Design
of
GAS-HANDLING
Systems
and
Facilities
Figure
10-5.
Integral
engine
compr...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 3 potx
... Design
of
GAS-HANDLING
Systems
and
Facilities
tlon
and
discharge valves
so
that
the
valves
can be
removed
and
rein-
stalled.
These clearances
are
called
fixed
clearances
and ... contains
the
rotating
parts
and on
which
the
cylinders
and
crossheads
are
mounted.
(Courtesy
of
Dresser-Rand
Company .)
310
Design
of
GAS-HANDLING
Systems...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 4 pdf
... 7,500
16, 300
18,800
17,700
17,700
17,400
16, 300
17,500
16, 300
17,500
11 ,20 0
—
12, 300
10 ,20 0
18,300
20 ,000
21
700
23 ,300
15,000
16, 700
18,100
1
6, 900
18,300
18,300
20 ,000
20 ,000
20 ,000
20 ,000
23 ,300
21 ,700
25 ,000
25 ,000
25 ,000
25 .000
21 .700
23 ,300
21 ,700
23 ,300
20 ,000
16, 700
20 ,000
16, 700
Wall
... 1.1
Class
150
300
400
60 0
900
1500...
ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 5 pps
... (17,50 0) (0.8 5)
-
(0. 2) ( 12 5)
Required
thickness
=
0.505
+
0 .25 0
=
0.755
in.
Use—-in.
head (0.8 12 5)
W
=
(0.3 4)( 0.8 12 5)( 12 0)
2
+
(1. 9)( 0.8 12 5)( 12 0)
=
4, 163 1b
(c)
Cone:
_
Pd
~
2
... Examined
Examined
3
1.00
0.85 0.70
0.90
0.80 0 .65
—
0 .60
—
—
0.55
on
page)
3 52
Design
of
GAS-HANDLING
Systems
and...
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