| 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 |
| 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 |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
|---|---|
| Pore Size | Uniform Pore Size Distribution |
| Stability | Excellent Stability Under Harsh Conditions |
| Particle Size | Narrow Particle Size Distribution |
| Operating Temperature | 30-35°C |
| Catalyst Type | Supported Metal Catalyst |
|---|---|
| Pore Size | Uniform Pore Size Distribution |
| Selectivity | High Selectivity C3 Hydrogenation |
| Stability | Excellent Stability Under Harsh Conditions |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Support Material | Alumina |
|---|---|
| Pressure | 3.5MPa |
| Industry | Chemical Industry |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
| 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 |
|---|---|
| Particle Size | 3-4.5 Mm |
| Industry | Chemical Industry |
| Pressure | 3.5MPa |
| Support Material | Alumina |
| Operating Temperature | 150-250°C |
|---|---|
| Shape | Spherical |
| Activity | >90% |
| Pore Size | 8-12 Nm |
| Pore Volume | 0.3-0.5 ML/g |
| Active Metal | Palladium |
|---|---|
| Catalyst Type | Heterogeneous |
| Thermal Stability | High |
| Particle Size | 1-3 Mm |
| Selectivity | >95% |