| Support Material | Aluminum Oxide (Al2O3) |
|---|---|
| Stability | Excellent Stability Under Harsh Conditions |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Catalyst Type | Supported Metal Catalyst |
| Particle Size | Narrow Particle Size Distribution |
| Selectivity | 80% |
|---|---|
| Particle Size | 3-4.5 Mm |
| Pore Volume | 0.85-0.95 Cm3/g |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
| Shelf Life | 2 Years |
|---|---|
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Solubility | Insoluble In Water |
| Shape | Spherical |
|---|---|
| Size | 1-3 Mm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Pore Size | 0.3-0.5 Nm |
| Surface Area | 150-200 M2/g |
| 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 |
| Reusability | Yes |
|---|---|
| Pressure | 3.5MPa |
| Particle Size | 3-4.5 Mm |
| Industry | Chemical Industry |
| Pore Volume | 0.85-0.95 Cm3/g |
| Pore Size | 0.3-0.5 Nm |
|---|---|
| Surface Area | 150-200 M2/g |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Bulk Density | 0.7-0.9 G/cm3 |
| Reaction Selectivity | 95-98% |
| Density | 0.55 G/cm3 |
|---|---|
| Solubility | Insoluble In Water |
| Purity | ≥ 98% |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Storage | Store In Dry Place |
| Industry | Chemical Industry |
|---|---|
| Support Material | Alumina |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
| Selectivity | 80% |
| Regenerability | Can Be Regenerated Multiple Times Without Significant Loss Of Activity |
|---|---|
| Stability | Excellent Stability Under Harsh Conditions |
| Pore Size | Uniform Pore Size Distribution |
| Operating Temperature | 30-35°C |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |