Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
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Particle Size | 1-3 Mm |
Appearance | Dark Gray To Black Solid |
Promoter | Aluminum Oxide (Al2O3) |
Active Component | Palladium (Pd) |
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 |
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 |
Active Metal | Palladium |
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Particle Size | 3-4.5 Mm |
Industry | Chemical Industry |
Pressure | 3.5MPa |
Support Material | Alumina |
Reaction Selectivity | 95-98% |
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Pore Size | 0.3-0.5 Nm |
Catalyst Life | 2-3 Years |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Bulk Density | 0.7-0.9 G/cm3 |
Active Component | Palladium (Pd) |
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Pore Volume | 0.3-0.5 Cm3/g |
Promoter | Aluminum Oxide (Al2O3) |
Appearance | Dark Gray To Black Solid |
Surface Area | 100-200 M2/g |
Support Material | Alumina |
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Pressure | 3.5MPa |
Industry | Chemical Industry |
Surface Area | 150-200 M2/g |
Shape | Spherical |
Active Component | Pd, Pt, Ni, Or Co |
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Particle Size | 1.5-3.0 Mm |
Support Material | Alumina Or Silica-alumina |
Active Component Loading | ≥ 2 Wt% |
Operating Temperature | 150-250°C |
Density | 0.55 G/cm3 |
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Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Purity | ≥ 98% |
Storage | Store In Dry Place |
Shelf Life | 2 Years |
Support Material | Aluminum Oxide (Al2O3) |
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Particle Size | Narrow Particle Size Distribution |
Pore Size | Uniform Pore Size Distribution |
Application | Selective Hydrogenation Of C3 Hydrocarbons |
Regenerability | Can Be Regenerated Multiple Times Without Significant Loss Of Activity |