Composition | Nickel, Cobalt, Molybdenum, Alumina |
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Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
---|---|
Bulk Density | 0.7-0.9 G/cm3 |
Application | Hydrogenation Of Cracked Gasoline |
Reaction Selectivity | 95-98% |
Size | 1-3 Mm |
Pore Volume | 0.58-0.66 Cm3/g |
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Shape | Spherical |
Heat Stability | High |
Lifespan | 4-5 Years |
Product Type | Solid Catalyst |
Pore Volume | 0.58-0.66 Cm3/g |
---|---|
Heat Stability | High |
Product Type | Solid Catalyst |
Lifespan | 4-5 Years |
Surface Area | 190-200 M2/g |
Application | Selective Hydrogenation Of C2 |
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Industry | Chemical Industry |
Shape | Spherical |
Support Material | Alumina |
Operating Temperature | 60-100°C |
Lifespan | 4-5 Years |
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Heat Stability | High |
Surface Area | 190-200 M2/g |
Shape | Spherical |
Size | 1.6-1.8 Mm |
Pore Volume | 0.6-0.8 Cm3/g |
---|---|
Na2O Content | ≤0.2% |
Surface Area | 100-110 M2/g |
Mgo Content | ≤0.05% |
Thermal Stability | Up To 1200℃ |
Surface Area | 190-200 M2/g |
---|---|
Size | 1.6-1.8 Mm |
Heat Stability | High |
Shape | Spherical |
Lifespan | 4-5 Years |
Chemical Stability | Acid And Alkali Resistant |
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Shape | Sphere |
Pore Size | 8-015nm |
Thermal Stability | ≥570℃ |
Crushing Strength | ≥40N |
Size | 1-3 Mm |
---|---|
Reaction Selectivity | 95-98% |
Pore Size | 0.3-0.5 Nm |
Catalyst Life | 2-3 Years |
Application | Hydrogenation Of Cracked Gasoline |