PURIFICATION OF HYDROGEN
CONTAINING GASES
|
TYPE
|
METAL
|
SIZE (mm)
|
DENSITY (KG/L)
|
APPLICATION
|
COMMENTS
|
|
D
|
0.5% Pd
|
3 Dia x 3 Cyl.
|
1.0
|
Removal of O2
|
|
|
DS2
|
0.2% Pd
|
2 to 5 Sph.
|
0.9
|
Removal of O2
|
Standard choice for this application
|
|
DSL2
|
0.2% Pd
|
2 to 5 Sph.
|
0.6
|
Removal of O2
|
Most economic choice.
|
|
DK
|
0.5% Pd
|
3 Dia x 3 Cyl
|
1.0
|
Removal of O2
|
High crush strength. Good resistance to
dusting.
|
|
E
|
0.15% Ru
|
3 Dia x 3 Cyl
|
1.0
|
Methanation of CO. Removal of H2O2
|
Historic choice
|
PURIFICATION OF OXYGEN
CONTAINING GASES
|
DSS3
|
0.3% Pd
|
4 to 6 Sph.
|
0.76
|
Oxidation of methane and hydrocarbons
|
Low light-off temperature
(300-350oC)
|
|
M
|
0.5% Pt
|
3 Dia x 3 Cyl
|
1.0
|
Removal of H2,CO and hydrocarbons
|
Historic choice
|
|
M3
|
0.3% Pt
|
3 Dia x 3 Cyl
|
1.0
|
Removal of H2,CO and hydrocarbons
|
Competitive price. Choice if poisons present.
|
|
MS2
|
0.2% Pt
|
2 to 5 Sph.
|
0.9
|
Removal of H2,CO and hydrocarbons
|
Most economic choice.
|
|
MSL15
|
0.15% Pt
|
2 to 4 Sph.
|
0.6
|
Air purification
|
Competitive price. Standard choice for
this application
|
The following information is available on request:
Recommended quantity
Recommended bed dimensions
Pressure drop
Temperature rise
Outlet purity gurantee
