| 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 |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
|---|---|
| Application | Hydrogenation Of Cracked Gasoline |
| Bulk Density | 0.7-0.9 G/cm3 |
| Size | 1-3 Mm |
| Reaction Selectivity | 95-98% |
| Reaction Selectivity | 95-98% |
|---|---|
| Pore Size | 0.3-0.5 Nm |
| Catalyst Life | 2-3 Years |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Bulk Density | 0.7-0.9 G/cm3 |
| Support Material | Alumina Or Silica-alumina |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Bulk Density | 0.65-0.75 G/cm3 |
| Support Material Content | ≥ 90 Wt% |
| Hydrogenation Selectivity | ≥ 95% |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
|---|---|
| Surface Area | 100-200 M2/g |
| Appearance | Dark Gray To Black Solid |
| Active Component | Palladium (Pd) |
| Particle Size | 1-3 Mm |
| 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 |
| 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 |
| 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% |
| Pore Size | 0.3-0.5 Nm |
| Catalyst Life | 2-3 Years |
| Application | Hydrogenation Of Cracked Gasoline |
| 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 |
