| 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 |
| Active Metal | Palladium |
|---|---|
| Particle Size | 3-4.5 Mm |
| Industry | Chemical Industry |
| Pressure | 3.5MPa |
| Support Material | Alumina |
| Density | 0.55 G/cm3 |
|---|---|
| Solubility | Insoluble In Water |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Storage | Store In Dry Place |
| Purity | ≥ 98% |
| Density | 0.55 G/cm3 |
|---|---|
| Solubility | Insoluble In Water |
| Purity | ≥ 98% |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Storage | Store In Dry Place |
| Pore Volume | 0.85-0.95 Cm3/g |
|---|---|
| Shape | Spherical |
| Pressure | 3.5MPa |
| Selectivity | 80% |
| Support Material | Alumina |
| Storage | Store In Dry Place |
|---|---|
| Purity | ≥ 98% |
| Shelf Life | 2 Years |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Solubility | Insoluble In Water |
| Particle Size | 3-4.5 Mm |
|---|---|
| Support Material | Alumina |
| Shape | Spherical |
| Pressure | 3.5MPa |
| Industry | Chemical Industry |
| 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 |
| Shape | Spherical |
|---|---|
| Stability | Excellent Stability Under Harsh Conditions |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Pore Size | Uniform Pore Size Distribution |
| Selectivity | High Selectivity C3 Hydrogenation |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
|---|---|
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
| Size | 1-3 Mm |
| Pore Size | 0.3-0.5 Nm |