| Reusability | Yes | 
|---|---|
| Pore Volume | 0.85-0.95 Cm3/g | 
| Support Material | Alumina | 
| Pressure | 3.5MPa | 
| Industry | Chemical Industry | 
| 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 | 
| 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 | Alumina | 
|---|---|
| Pressure | 3.5MPa | 
| Industry | Chemical Industry | 
| Surface Area | 150-200 M2/g | 
| Shape | Spherical | 
| Shape | Spherical | 
|---|---|
| Surface Area | 150-200 M2/g | 
| Pore Volume | 0.85-0.95 Cm3/g | 
| Selectivity | 80% | 
| Industry | Chemical Industry | 
| Reusability | Yes | 
|---|---|
| Support Material | Alumina | 
| Operating Temperature | 60-100°C | 
| Selectivity | 80% | 
| Surface Area | 150-200 M2/g | 
| Shape | Spherical | 
|---|---|
| Stability | Excellent Stability Under Harsh Conditions | 
| Surface Area | High Surface Area For Efficient Catalytic Activity | 
| Pore Size | Uniform Pore Size Distribution | 
| Selectivity | High Selectivity C3 Hydrogenation | 
| Stability | Excellent Stability Under Harsh Conditions | 
|---|---|
| Operating Temperature | 30-35°C | 
| Pore Size | Uniform Pore Size Distribution | 
| Application | Selective Hydrogenation Of C3 Hydrocarbons | 
| Active Metal | Palladium (Pd) | 
| Active Metal | Palladium | 
|---|---|
| Particle Size | 3-4.5 Mm | 
| Industry | Chemical Industry | 
| Pressure | 3.5MPa | 
| Support Material | Alumina | 
| Bulk Density | 0.65-0.75 G/cm3 | 
|---|---|
| Particle Size | 1.5-3.0 Mm | 
| Operating Temperature | 150-250°C | 
| Operating Pressure | 1-10 MPa | 
| Active Component | Pd, Pt, Ni, Or Co |