... Anti-Agglomerators,
10 7
CHAPTER
S
LTX
Units
and
Line Heaters
10 9
LTX
Units,
11 0
Line
Heaters,
11 2
Heat Duty,
11 3
Fire-Tube
Size,
11 5
Coil
Sizing,
11 6
Choose
Temperatures
11 6,
Choose ... modern
and
common
practices.
We
have
either
personally
been
involved
in the
design
and
troubleshooting
of
facilities throughout
xiii
10
Design
of...
... on 1%
hydrogen
sulfide
=
629 .77
gr /10 0
scfat
14 .696
psia
and
59°F,
or
10 1,325
kPa
and
75 °C.
15 6
Design
of
GAS-HANDLING
Systems
and
Facilities
(text
continued from page
15 3)
GAS
... threat-
*Reviewed
for the
19 99 edition
by K. S.
Chiou
of
Paragon Engineering Services, Inc.
15 1
15 2
Design
of
GAS-HANDLING
Systems
and
Fa...
... rate
of
deposition
of 15
grains
of
H
2
S/min/ft
2
of bed
cross-sectional area
is
also recommended
to
allow
for the
dissipation
of
17 6
Design
of
GAS-HANDLING
Systems
and
Facilities
Figure
... developed
and
patented
by
NL
Treating Chemicals
and is now a
product
of
Exxon Energy
Chem-
16 2
Design
of
GAS-HANDLING
Systems
and
Facili...
... rate
Figure
8 -9.
Equilibrium
water
dew
points
at
different
temperatures
for
gases.
19 2
Design
of
GAS-HANDLING
Systems
and
Facilities
ci
H
in.
_ft_
18
1. 9. 2
20
15 ,5
22
12 .8
24
10 .8
30
... a
pressure
of
3,000
psia
and a
temperature
of
15 0°R
From Figure
8 -1 at a
temperature
of
15 0°F
and
pressure
of
3,000
psia there
is...
... reduction
and
the
other
one for
oxidation.
The
oxidation process
with
CO
takes place
as;
2CO +
O
2
<-»
2CO
2
The
oxidation
of UHC is:
2O
2
+
CH
4
<-»
CO
2
+
2H
2
O
And
finally,
... reduction
of
NO
X
with
CO
results
in
N
2
and
CO
2
:
NO
2
+ CO
<-»
NO +
CO
2
2NO + 2CO
<-»
N
2
+
2CO
2
Catalytic reactions occur when
the
t...