| Operating Pressure | 1-10 MPa |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Pore Diameter | 30-80 Å |
| Appearance | Gray Or Black Cylindrical Particles |
| Particle Size | 1.5-3.0 Mm |
| Support Material | Alumina |
|---|---|
| Active Metal | Palladium |
| Operating Temperature | 60-100°C |
| Shape | Spherical |
| Particle Size | 3-4.5 Mm |
| Selectivity | 80% |
|---|---|
| Support Material | Alumina |
| Surface Area | 150-200 M2/g |
| Active Metal | Palladium |
| Application | Selective Hydrogenation Of C2 |
| Support Material | Alumina |
|---|---|
| Pressure | 3.5MPa |
| Industry | Chemical Industry |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
| Lifetime | 3-4 Years |
|---|---|
| Size | 1.6 Mm |
| Bulk Density | 0.62 G/cm3 |
| Pore Size | 20 Nm |
| Material | Platinum |
| Lifetime | 3-4 Years |
|---|---|
| Product Type | Catalyst |
| Shape | Pellet |
| Surface Area | 100 M2/g |
| Size | 1.6 Mm |
| Bulk Density | 0.65-0.75 G/cm3 |
|---|---|
| Catalyst Lifespan | ≥ 3 Years |
| Surface Area | ≥ 150 M2/g |
| Hydrogenation Selectivity | ≥ 95% |
| Operating Pressure | 1-10 MPa |
| Selectivity | 80% |
|---|---|
| Surface Area | 150-200 M2/g |
| Reusability | Yes |
| Industry | Chemical Industry |
| Shape | Spherical |
| 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 |
| Industry | Chemical Industry |
|---|---|
| Pressure | 3.5MPa |
| Active Metal | Palladium |
| Reusability | Yes |
| Selectivity | 80% |