Catalyst Type | Supported Metal Catalyst |
---|---|
Particle Size | Narrow Particle Size Distribution |
Shape | Spherical |
Activity | High Activity For C3 Hydrogenation |
Active Metal | Palladium (Pd) |
Support Material | Aluminum Oxide (Al2O3) |
---|---|
Selectivity | High Selectivity C3 Hydrogenation |
Catalyst Type | Supported Metal Catalyst |
Stability | Excellent Stability Under Harsh Conditions |
Activity | High Activity For C3 Hydrogenation |
Reusability | Yes |
---|---|
Pressure | 3.5MPa |
Particle Size | 3-4.5 Mm |
Industry | Chemical Industry |
Pore Volume | 0.85-0.95 Cm3/g |
Surface Area | 100 M2/g |
---|---|
Operating Temperature | 550-650°C |
Product Type | Catalyst |
Size | 1.6 Mm |
Bulk Density | 0.62 G/cm3 |
Application | Petrochemical Industry |
---|---|
Product Type | Catalyst |
Material | Platinum |
Pore Size | 20 Nm |
Catalyst Loading | 0.63 Kg/m3 |
Material | Platinum |
---|---|
Operating Temperature | 550-650°C |
Surface Area | 100 M2/g |
Lifetime | 3-4 Years |
Shape | Pellet |
Catalyst Loading | 0.63 Kg/m3 |
---|---|
Lifetime | 3-4 Years |
Material | Platinum |
Surface Area | 100 M2/g |
Pore Size | 20 Nm |
Shape | Pellet |
---|---|
Size | 1.6 Mm |
Product Type | Catalyst |
Catalyst Loading | 0.63 Kg/m3 |
Material | Platinum |
Operating Temperature | 550-650°C |
---|---|
Catalyst Loading | 0.63 Kg/m3 |
Bulk Density | 0.62 G/cm3 |
Application | Petrochemical Industry |
Product Type | Catalyst |
Support Material | Alumina Or Silica-alumina |
---|---|
Catalyst Lifespan | ≥ 3 Years |
Pore Diameter | 30-80 Å |
Pore Volume | ≥ 0.35 ML/g |
Active Component | Pd, Pt, Ni, Or Co |