Hydrogenation Cat
HS103 Organic Sulfur Hydrogenation Catalyst
|
Application
Hydrogenation for removal of organic sulfur in refinery gas, coking gas and water gas containing high CO and CO2, especially applying in coke dry gas containing olefin as high as approx. 7% to protect normal function of various catalysts in downstream.
Characteristics
γ-Al2O3 carrier with Ni, Co and Mo as the active ingredients
Physical and chemical properties
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Appearance
|
Gray blue spheres
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|
Size, mm
|
Φ2-4
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|
Bulk Density, kg/l
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0.6-0.7
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Crushing Strength, N/cm
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≥50
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|
Components
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Ni, Co, Mo, γ-Al2O3
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|
Attrition loss, %
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≤3.0
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Operating Conditions
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Inlet feedstock
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Organic sulfur≤200ppm, olefin≤7%, H2≥20%
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|
Inlet temperature, °C
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200-280
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|
Pressure, MPa
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0-5.0
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|
Space Velocity, h-1
|
1000-1500
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|
Outlet feedstock
|
Organic sulfur≤0.1ppm, olefin≤0.1%
|
|
|
| [Back] |
HS103 Organic Sulfur Hydrogenation Catalyst
|
Application
Hydrogenation for removal of organic sulfur in refinery gas, coking gas and water gas containing high CO and CO2, especially applying in coke dry gas containing olefin as high as approx. 7% to protect normal function of various catalysts in downstream.
Characteristics
γ-Al2O3 carrier with Ni, Co and Mo as the active ingredients
Physical and chemical properties
|
Appearance
|
Gray blue spheres
|
|
Size, mm
|
Φ2-4
|
|
Bulk Density, kg/l
|
0.6-0.7
|
|
Crushing Strength, N/cm
|
≥50
|
|
Components
|
Ni, Co, Mo, γ-Al2O3
|
|
Attrition loss, %
|
≤3.0
|
Operating Conditions
|
Inlet feedstock
|
Organic sulfur≤200ppm, olefin≤7%, H2≥20%
|
|
Inlet temperature, °C
|
200-280
|
|
Pressure, MPa
|
0-5.0
|
|
Space Velocity, h-1
|
1000-1500
|
|
Outlet feedstock
|
Organic sulfur≤0.1ppm, olefin≤0.1%
|
|
|
| [Back] |
