Catalyst Loading | 0.63 Kg/m3 |
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Product Type | Catalyst |
Pore Size | 20 Nm |
Material | Platinum |
Lifetime | 3-4 Years |
Pore Volume | 0.58-0.66 Cm3/g |
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Shape | Spherical |
Product Type | Solid Catalyst |
Size | 1.6-1.8 Mm |
Heat Stability | High |
Catalyst Life | 2-3 Years |
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Bulk Density | 0.7-0.9 G/cm3 |
Application | Hydrogenation Of Cracked Gasoline |
Pore Size | 0.3-0.5 Nm |
Size | 1-3 Mm |
Surface Area | 100 M2/g |
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Operating Temperature | 550-650°C |
Product Type | Catalyst |
Size | 1.6 Mm |
Bulk Density | 0.62 G/cm3 |
Bulk Density | 0.62 G/cm3 |
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Catalyst Loading | 0.63 Kg/m3 |
Pore Size | 20 Nm |
Lifetime | 3-4 Years |
Application | Petrochemical Industry |
Catalyst Lifespan | ≥ 3 Years |
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Active Component | Pd, Pt, Ni, Or Co |
Particle Size | 1.5-3.0 Mm |
Hydrogenation Selectivity | ≥ 95% |
Pore Volume | ≥ 0.35 ML/g |
Shape | Spherical |
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Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Reaction Selectivity | 95-98% |
Size | 1-3 Mm |
Industry | Chemical Industry |
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Support Material | Alumina |
Surface Area | 150-200 M2/g |
Shape | Spherical |
Selectivity | 80% |
Particle Size | 1-3 Mm |
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Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
Promoter | Aluminum Oxide (Al2O3) |
Surface Area | 100-200 M2/g |
Active Component | Palladium (Pd) |
Shape | Pellet |
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Operating Temperature | 550-650°C |
Product Type | Catalyst |
Size | 1.6 Mm |
Lifetime | 3-4 Years |