Pore Volume | 0.85-0.95 Cm3/g |
---|---|
Shape | Spherical |
Pressure | 3.5MPa |
Selectivity | 80% |
Support Material | Alumina |
Storage | Store In Dry Place |
---|---|
Purity | ≥ 98% |
Shelf Life | 2 Years |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Solubility | Insoluble In Water |
Particle Size | 3-4.5 Mm |
---|---|
Support Material | Alumina |
Shape | Spherical |
Pressure | 3.5MPa |
Industry | Chemical Industry |
Surface Area | 150-200 M2/g |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Shape | Spherical |
---|---|
Stability | Excellent Stability Under Harsh Conditions |
Surface Area | High Surface Area For Efficient Catalytic Activity |
Pore Size | Uniform Pore Size Distribution |
Selectivity | High Selectivity C3 Hydrogenation |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
---|---|
Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Pore Size | 0.3-0.5 Nm |
Surface Area | 150-200 M2/g |
---|---|
Shape | Spherical |
Active Metal | Palladium |
Reusability | Yes |
Operating Temperature | 60-100°C |
Regenerability | Can Be Regenerated Multiple Times Without Significant Loss Of Activity |
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Stability | Excellent Stability Under Harsh Conditions |
Pore Size | Uniform Pore Size Distribution |
Operating Temperature | 30-35°C |
Application | Selective Hydrogenation Of C3 Hydrocarbons |
Reaction Selectivity | 95-98% |
---|---|
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 |
Catalyst Type | Supported Metal Catalyst |
---|---|
Support Material | Aluminum Oxide (Al2O3) |
Activity | High Activity For C3 Hydrogenation |
Particle Size | Narrow Particle Size Distribution |
Application | Selective Hydrogenation Of C3 Hydrocarbons |