| Pore Size | 0.3-0.5 Nm |
|---|---|
| Application | Hydrogenation Of Cracked Gasoline |
| Shape | Spherical |
| Reaction Selectivity | 95-98% |
| Bulk Density | 0.7-0.9 G/cm3 |
| Purity | ≥ 98% |
|---|---|
| Solubility | Insoluble In Water |
| Shelf Life | 2 Years |
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
|---|---|
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Shelf Life | 2 Years |
| Solubility | Insoluble In Water |
| Active Metal | Palladium |
|---|---|
| Particle Size | 3-4.5 Mm |
| Industry | Chemical Industry |
| Pressure | 3.5MPa |
| Support Material | Alumina |
| Density | 0.55 G/cm3 |
|---|---|
| Solubility | Insoluble In Water |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Storage | Store In Dry Place |
| Purity | ≥ 98% |
| Pore Volume | 0.85-0.95 Cm3/g |
|---|---|
| Shape | Spherical |
| Pressure | 3.5MPa |
| Selectivity | 80% |
| Support Material | 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 |
| Surface Area | 150-200 M2/g |
|---|---|
| Shape | Spherical |
| Active Metal | Palladium |
| Reusability | Yes |
| Operating Temperature | 60-100°C |
| 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 |