| Application | Selective Hydrogenation Of C2 |
|---|---|
| Industry | Chemical Industry |
| Shape | Spherical |
| Support Material | Alumina |
| Operating Temperature | 60-100°C |
| 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 |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
|---|---|
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Shelf Life | 2 Years |
| Solubility | Insoluble In Water |
| 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 |
| Shape | Spherical |
|---|---|
| Pore Size | 0.3-0.5 Nm |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Reaction Selectivity | 95-98% |
| Size | 1-3 Mm |
| Storage | Store In Dry Place |
|---|---|
| Purity | ≥ 98% |
| Shelf Life | 2 Years |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Solubility | Insoluble In Water |
| 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 |
| 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 |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
|---|---|
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
| Size | 1-3 Mm |
| Pore Size | 0.3-0.5 Nm |
| Surface Area | 150-200 M2/g |
|---|---|
| Shape | Spherical |
| Active Metal | Palladium |
| Reusability | Yes |
| Operating Temperature | 60-100°C |