| Active Component | Palladium (Pd) |
|---|---|
| Pore Volume | 0.3-0.5 Cm3/g |
| Promoter | Aluminum Oxide (Al2O3) |
| Appearance | Dark Gray To Black Solid |
| Surface Area | 100-200 M2/g |
| 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 |
| 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 | 100-200 M2/g |
|---|---|
| Particle Size | 1-3 Mm |
| Active Component | Palladium (Pd) |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
| Promoter | Aluminum Oxide (Al2O3) |
| Catalyst Life | 2-3 Years |
|---|---|
| Bulk Density | 0.7-0.9 G/cm3 |
| Application | Hydrogenation Of Cracked Gasoline |
| Pore Size | 0.3-0.5 Nm |
| Size | 1-3 Mm |
| Bulk Density | 0.65-0.75 G/cm3 |
|---|---|
| Catalyst Lifespan | ≥ 3 Years |
| Surface Area | ≥ 150 M2/g |
| Hydrogenation Selectivity | ≥ 95% |
| Operating Pressure | 1-10 MPa |
| Active Component | Pd, Pt, Ni, Or Co |
|---|---|
| Particle Size | 1.5-3.0 Mm |
| Support Material | Alumina Or Silica-alumina |
| Active Component Loading | ≥ 2 Wt% |
| Operating Temperature | 150-250°C |
| Surface Area | 150-200 M2/g |
|---|---|
| Application | Hydrogenation Of Cracked Gasoline |
| Shape | Spherical |
| Pore Size | 0.3-0.5 Nm |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
|---|---|
| Particle Size | 1-3 Mm |
| Appearance | Dark Gray To Black Solid |
| Promoter | Aluminum Oxide (Al2O3) |
| Active Component | Palladium (Pd) |
| Promoter | Aluminum Oxide (Al2O3) |
|---|---|
| Active Component | Palladium (Pd) |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
| Surface Area | 100-200 M2/g |
| Pore Volume | 0.3-0.5 Cm3/g |