| Shape | Grey Brown Clover | 
|---|---|
| Material | Alumina | 
| Chemical Composition | Al2O3 | 
| Regenerability | Good | 
| Application | C3 Hydrogenation Catalyst For MAPD Removal | 
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons | 
|---|---|
| Pore Volume | 0.3-0.5 Cm3/g | 
| Surface Area | 100-200 M2/g | 
| Active Component | Palladium (Pd) | 
| Appearance | Dark Gray To Black Solid | 
| Catalyst Lifespan | ≥ 3 Years | 
|---|---|
| Active Component | Pd, Pt, Ni, Or Co | 
| Particle Size | 1.5-3.0 Mm | 
| Hydrogenation Selectivity | ≥ 95% | 
| Pore Volume | ≥ 0.35 ML/g | 
| Pore Size | 0.3-0.5 Nm | 
|---|---|
| Surface Area | 150-200 M2/g | 
| Composition | Nickel, Cobalt, Molybdenum, Alumina | 
| Bulk Density | 0.7-0.9 G/cm3 | 
| Reaction Selectivity | 95-98% | 
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons | 
|---|---|
| Appearance | Dark Gray To Black Solid | 
| Active Component | Palladium (Pd) | 
| Particle Size | 1-3 Mm | 
| Pore Volume | 0.3-0.5 Cm3/g | 
| Regenerability | Good | 
|---|---|
| Promoter | Aluminum Oxide (Al2O3) | 
| Pore Volume | 0.3-0.5 Cm3/g | 
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons | 
| Thermal Stability | High | 
| Surface Area | 100-200 M2/g | 
|---|---|
| Promoter | Aluminum Oxide (Al2O3) | 
| Appearance | Dark Gray To Black Solid | 
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons | 
| Particle 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 | 
| Pore Diameter | 30-80 Å | 
|---|---|
| Operating Pressure | 1-10 MPa | 
| Active Component Loading | ≥ 2 Wt% | 
| Support Material | Alumina Or Silica-alumina | 
| Pore Volume | ≥ 0.35 ML/g | 
| Catalyst Life | 2-3 Years | 
|---|---|
| Pore Size | 0.3-0.5 Nm | 
| Reaction Selectivity | 95-98% | 
| Application | Hydrogenation Of Cracked Gasoline | 
| Size | 1-3 Mm |