Sulfur Adsorbent
EH-3 Sulfur-Tolerant Hydrolysis Catalyst
Application
EH-2/EH-3 has been applied in high COS, CS2 and H2S feedstock before CO2 removal system in ammonia or methanol plants to hydrolyze COS to H2S.
Characteristics
EH-2/EH-3 can ensure COS and CS2 reach near equilibrium conversion ratio.
Physical and chemical properties
|
EH-2
|
EH-3
|
Appearance
|
White sphere
|
Light green sphere
|
Size, mm
|
Φ3.0-6.0
|
Bulk Density, kg/l
|
0.8-1.0
|
Crushing Strength, N/Point
|
≥25
|
Operating Conditions
|
EH-2
|
EH-3
|
Temperature, °C
|
160-250
|
Pressure, MPa
|
≤15.0
|
Space Velocity, h-1
|
1000-3000
|
COS, CS2 conversion ratio
|
Near equilibrium value
|
Inlet H2 content, %
|
≥10
|
Inlet O2 content, ppm
|
≤1000
|
≤6000
|
|
|
[Back] |
EH-3 Sulfur-Tolerant Hydrolysis Catalyst
Application
EH-2/EH-3 has been applied in high COS, CS2 and H2S feedstock before CO2 removal system in ammonia or methanol plants to hydrolyze COS to H2S.
Characteristics
EH-2/EH-3 can ensure COS and CS2 reach near equilibrium conversion ratio.
Physical and chemical properties
|
EH-2
|
EH-3
|
Appearance
|
White sphere
|
Light green sphere
|
Size, mm
|
Φ3.0-6.0
|
Bulk Density, kg/l
|
0.8-1.0
|
Crushing Strength, N/Point
|
≥25
|
Operating Conditions
|
EH-2
|
EH-3
|
Temperature, °C
|
160-250
|
Pressure, MPa
|
≤15.0
|
Space Velocity, h-1
|
1000-3000
|
COS, CS2 conversion ratio
|
Near equilibrium value
|
Inlet H2 content, %
|
≥10
|
Inlet O2 content, ppm
|
≤1000
|
≤6000
|
|
|
[Back] |