Hydrogenation Cat
HS102 Organic Sulfur Hydrogenation Catalyst
|
Application
Hydrogenation for removal of organic sulfur in coking gas which containing CO as high as approx. 8% and saturation of olefin contained in the gas to protect normal function of various catalysts in downstream.
Characteristics
γ-Al2O3 carrier with Fe and Mo as the active ingredients
Physical and chemical properties
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Appearance
|
Chocolate brown flake
|
|
Size, mm
|
Φ7.0×(5-6)
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|
Bulk Density, kg/l
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0.7-0.9
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|
Crushing Strength, N/cm
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≥47
|
|
MoO3 mass fraction, %
|
7.5-10.5
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|
Fe mass fraction, %
|
2.1-3.0
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Operating Conditions
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Inlet organic sulfur content, ppmv
|
200-300
|
|
Temperature, °C
|
350-420
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|
Pressure, MPa
|
1.6-4.0
|
|
Space Velocity, h-1
|
1000
|
|
Organic sulfur conversion ratio, %
|
≥96
|
|
|
| [Back] |
HS102 Organic Sulfur Hydrogenation Catalyst
|
Application
Hydrogenation for removal of organic sulfur in coking gas which containing CO as high as approx. 8% and saturation of olefin contained in the gas to protect normal function of various catalysts in downstream.
Characteristics
γ-Al2O3 carrier with Fe and Mo as the active ingredients
Physical and chemical properties
|
Appearance
|
Chocolate brown flake
|
|
Size, mm
|
Φ7.0×(5-6)
|
|
Bulk Density, kg/l
|
0.7-0.9
|
|
Crushing Strength, N/cm
|
≥47
|
|
MoO3 mass fraction, %
|
7.5-10.5
|
|
Fe mass fraction, %
|
2.1-3.0
|
Operating Conditions
|
Inlet organic sulfur content, ppmv
|
200-300
|
|
Temperature, °C
|
350-420
|
|
Pressure, MPa
|
1.6-4.0
|
|
Space Velocity, h-1
|
1000
|
|
Organic sulfur conversion ratio, %
|
≥96
|
|
|
| [Back] |
