| 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 |
| Surface Area | 150-200 M2/g |
|---|---|
| Industry | Chemical Industry |
| Pressure | 3.5MPa |
| Selectivity | 80% |
| Application | Selective Hydrogenation Of C2 |
| Support Material | Alumina |
|---|---|
| Active Metal | Palladium |
| Operating Temperature | 60-100°C |
| Shape | Spherical |
| Particle Size | 3-4.5 Mm |
| Shape | Spherical |
|---|---|
| Pore Size | Uniform Pore Size Distribution |
| Activity | High Activity For C3 Hydrogenation |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |
| Active Metal | Palladium |
|---|---|
| Catalyst Type | Heterogeneous |
| Thermal Stability | High |
| Particle Size | 1-3 Mm |
| Selectivity | >95% |
| Size | 1-3 Mm |
|---|---|
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
| Pore Size | 0.3-0.5 Nm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Catalyst Lifespan | ≥ 3 Years |
|---|---|
| Appearance | Gray Or Black Cylindrical Particles |
| Operating Pressure | 1-10 MPa |
| Particle Size | 1.5-3.0 Mm |
| Active Component | Pd, Pt, Ni, Or Co |
| 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% |
| Catalyst Life | 2-3 Years |
|---|---|
| Pore Size | 0.3-0.5 Nm |
| Reaction Selectivity | 95-98% |
| Application | Hydrogenation Of Cracked Gasoline |
| Size | 1-3 Mm |