Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
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Purity | ≥ 98% |
Solubility | Insoluble In Water |
Storage | Store In Dry Place |
Density | 0.55 G/cm3 |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
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Application | Hydrogenation Of Cracked Gasoline |
Bulk Density | 0.7-0.9 G/cm3 |
Size | 1-3 Mm |
Reaction Selectivity | 95-98% |
Surface Area | 150-200 M2/g |
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Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Bulk Density | 0.7-0.9 G/cm3 |
Bulk Density | 0.65-0.75 G/cm3 |
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Hydrogenation Selectivity | ≥ 95% |
Operating Temperature | 150-250°C |
Particle Size | 1.5-3.0 Mm |
Surface Area | ≥ 150 M2/g |
Catalyst Lifespan | ≥ 3 Years |
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Appearance | Gray Or Black Cylindrical Particles |
Operating Pressure | 1-10 MPa |
Particle Size | 1.5-3.0 Mm |
Active Component | Pd, Pt, Ni, Or Co |
Active Component Loading | ≥ 2 Wt% |
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Pore Volume | ≥ 0.35 ML/g |
Active Component | Pd, Pt, Ni, Or Co |
Pore Diameter | 30-80 Å |
Support Material Content | ≥ 90 Wt% |
Surface Area | High Surface Area For Efficient Catalytic Activity |
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Pore Size | Uniform Pore Size Distribution |
Stability | Excellent Stability Under Harsh Conditions |
Particle Size | Narrow Particle Size Distribution |
Operating Temperature | 30-35°C |
Shape | Spherical |
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Support Material | Aluminum Oxide (Al2O3) |
Activity | High Activity For C3 Hydrogenation |
Surface Area | High Surface Area For Efficient Catalytic Activity |
Selectivity | High Selectivity C3 Hydrogenation |
Catalyst Type | Supported Metal Catalyst |
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Pore Size | Uniform Pore Size Distribution |
Selectivity | High Selectivity C3 Hydrogenation |
Stability | Excellent Stability Under Harsh Conditions |
Surface Area | High Surface Area For Efficient Catalytic Activity |
Catalyst Type | Supported Metal Catalyst |
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Particle Size | Narrow Particle Size Distribution |
Shape | Spherical |
Activity | High Activity For C3 Hydrogenation |
Active Metal | Palladium (Pd) |