Selectivity | 80% |
---|---|
Particle Size | 3-4.5 Mm |
Pore Volume | 0.85-0.95 Cm3/g |
Surface Area | 150-200 M2/g |
Shape | Spherical |
Reusability | Yes |
---|---|
Pressure | 3.5MPa |
Particle Size | 3-4.5 Mm |
Industry | Chemical Industry |
Pore Volume | 0.85-0.95 Cm3/g |
Industry | Chemical Industry |
---|---|
Support Material | Alumina |
Surface Area | 150-200 M2/g |
Shape | Spherical |
Selectivity | 80% |
Active Metal | Palladium (Pd) |
---|---|
Particle Size | Narrow Particle Size Distribution |
Support Material | Aluminum Oxide (Al2O3) |
Activity | High Activity For C3 Hydrogenation |
Surface Area | High Surface Area For Efficient Catalytic Activity |
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 |
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 |
Shape | Spherical |
---|---|
Pore Size | Uniform Pore Size Distribution |
Selectivity | High Selectivity C3 Hydrogenation |
Active Metal | Palladium (Pd) |
Application | Selective Hydrogenation Of C3 Hydrocarbons |
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 |
Active Component Loading | ≥ 2 Wt% |
---|---|
Active Component | Pd, Pt, Ni, Or Co |
Hydrogenation Selectivity | ≥ 95% |
Support Material Content | ≥ 90 Wt% |
Operating Temperature | 150-250°C |