| 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 |
| 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 |
| 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 |
| Reusability | Yes |
|---|---|
| Pressure | 3.5MPa |
| Particle Size | 3-4.5 Mm |
| Industry | Chemical Industry |
| Pore Volume | 0.85-0.95 Cm3/g |
| Surface Area | 100 M2/g |
|---|---|
| Operating Temperature | 550-650°C |
| Product Type | Catalyst |
| Size | 1.6 Mm |
| Bulk Density | 0.62 G/cm3 |
| Application | Petrochemical Industry |
|---|---|
| Product Type | Catalyst |
| Material | Platinum |
| Pore Size | 20 Nm |
| Catalyst Loading | 0.63 Kg/m3 |
| Bulk Density | 0.62 G/cm3 |
|---|---|
| Catalyst Loading | 0.63 Kg/m3 |
| Pore Size | 20 Nm |
| Lifetime | 3-4 Years |
| Application | Petrochemical Industry |
| 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 |
| 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 |
|---|---|
| Pore Size | 0.3-0.5 Nm |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Reaction Selectivity | 95-98% |
| Size | 1-3 Mm |