| Composition | Nickel, Cobalt, Molybdenum, Alumina |
|---|---|
| Bulk Density | 0.7-0.9 G/cm3 |
| Application | Hydrogenation Of Cracked Gasoline |
| Reaction Selectivity | 95-98% |
| Size | 1-3 Mm |
| Surface Area | 150-200 M2/g |
|---|---|
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
| Size | 1-3 Mm |
| Bulk Density | 0.7-0.9 G/cm3 |
| 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 Life | 2-3 Years |
|---|---|
| Reaction Selectivity | 95-98% |
| Application | Hydrogenation Of Cracked Gasoline |
| Pore Size | 0.3-0.5 Nm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Shape | Spherical |
|---|---|
| Support Material | Aluminum Oxide (Al2O3) |
| Activity | High Activity For C3 Hydrogenation |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Selectivity | High Selectivity C3 Hydrogenation |
| 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 |
| Shape | Spherical |
|---|---|
| Size | 1-3 Mm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Pore Size | 0.3-0.5 Nm |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
|---|---|
| Pore Size | 0.3-0.5 Nm |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Reaction Selectivity | 95-98% |
| Size | 1-3 Mm |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |
|---|---|
| Particle Size | Narrow Particle Size Distribution |
| Catalyst Type | Supported Metal Catalyst |
| Selectivity | High Selectivity C3 Hydrogenation |
| Support Material | Aluminum Oxide (Al2O3) |
| Catalyst Type | Supported Metal Catalyst |
|---|---|
| Particle Size | Narrow Particle Size Distribution |
| Shape | Spherical |
| Activity | High Activity For C3 Hydrogenation |
| Active Metal | Palladium (Pd) |
