| Support Material | Alumina Or Silica-alumina |
|---|---|
| Catalyst Lifespan | ≥ 3 Years |
| Pore Diameter | 30-80 Å |
| Pore Volume | ≥ 0.35 ML/g |
| Active Component | Pd, Pt, Ni, Or Co |
| Shape | Spherical |
|---|---|
| Pore Size | 0.3-0.5 Nm |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Reaction Selectivity | 95-98% |
| Size | 1-3 Mm |
| Lifespan | 4-5 Years |
|---|---|
| Surface Area | 190-200 M2/g |
| Product Type | Solid Catalyst |
| Heat Stability | High |
| Size | 1.6-1.8 Mm |
| Appearance | Gray Or Black Cylindrical Particles |
|---|---|
| Operating Temperature | 150-250°C |
| Hydrogenation Selectivity | ≥ 95% |
| Catalyst Lifespan | ≥ 3 Years |
| Active Component Loading | ≥ 2 Wt% |
| 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 |
| Pore Volume | 0.58-0.66 Cm3/g |
|---|---|
| Shape | Spherical |
| Heat Stability | High |
| Lifespan | 4-5 Years |
| Product Type | Solid Catalyst |
| Pore Volume | 0.58-0.66 Cm3/g |
|---|---|
| Heat Stability | High |
| Product Type | Solid Catalyst |
| Lifespan | 4-5 Years |
| Surface Area | 190-200 M2/g |
| Application | Selective Hydrogenation Of C2 |
|---|---|
| Industry | Chemical Industry |
| Shape | Spherical |
| Support Material | Alumina |
| Operating Temperature | 60-100°C |
| Lifespan | 4-5 Years |
|---|---|
| Heat Stability | High |
| Surface Area | 190-200 M2/g |
| Shape | Spherical |
| Size | 1.6-1.8 Mm |
| Surface Area | 190-200 M2/g |
|---|---|
| Size | 1.6-1.8 Mm |
| Heat Stability | High |
| Shape | Spherical |
| Lifespan | 4-5 Years |
