| 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 |
| Particle Size | Narrow Particle Size Distribution |
|---|---|
| Pore Size | Uniform Pore Size Distribution |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |
| Stability | Excellent Stability Under Harsh Conditions |
| Operating Temperature | 60-100°C |
|---|---|
| Pressure | 3.5MPa |
| Selectivity | 80% |
| Active Metal | Palladium |
| Industry | Chemical Industry |
| Support Material | Alumina |
|---|---|
| Active Metal | Palladium |
| Operating Temperature | 60-100°C |
| Shape | Spherical |
| Particle Size | 3-4.5 Mm |
| Pore Volume | 0.85-0.95 Cm3/g |
|---|---|
| Shape | Spherical |
| Pressure | 3.5MPa |
| Selectivity | 80% |
| Support Material | Alumina |
| Pore Size | 0.3-0.5 Nm |
|---|---|
| Shape | Granular/spherical |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Bulk Density | 0.7-0.9 G/cm3 |
| Catalyst Life | 2-3 Years |
| Selectivity | 80% |
|---|---|
| Particle Size | 3-4.5 Mm |
| Pore Volume | 0.85-0.95 Cm3/g |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
| Industry | Chemical Industry |
|---|---|
| Support Material | Alumina |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
| Selectivity | 80% |
| Surface Area | 150-200 M2/g |
|---|---|
| Shape | Spherical |
| Active Metal | Palladium |
| Reusability | Yes |
| Operating Temperature | 60-100°C |
| Catalyst Type | Supported Metal Catalyst |
|---|---|
| Shape | Spherical |
| Activity | High Activity For C3 Hydrogenation |
| Stability | Excellent Stability Under Harsh Conditions |
| Pore Size | Uniform Pore Size Distribution |