| Surface Area | 150-200 M2/g |
|---|---|
| Industry | Chemical Industry |
| Pressure | 3.5MPa |
| Selectivity | 80% |
| Application | Selective Hydrogenation Of C2 |
| Support Material Content | ≥ 90 Wt% |
|---|---|
| Active Component | Pd, Pt, Ni, Or Co |
| Appearance | Gray Or Black Cylindrical Particles |
| Pore Diameter | 30-80 Å |
| Hydrogenation Selectivity | ≥ 95% |
| Active Component Loading | ≥ 2 Wt% |
|---|---|
| Active Component | Pd, Pt, Ni, Or Co |
| Hydrogenation Selectivity | ≥ 95% |
| Support Material Content | ≥ 90 Wt% |
| Operating Temperature | 150-250°C |
| Shape | Spherical |
|---|---|
| Lifetime | 3-4 Years |
| Catalyst Loading | 0.63 Kg/m3 |
| Product Type | Catalyst |
| Material | Platinum |
| Operating Temperature | 550-650°C |
|---|---|
| Product Type | Catalyst |
| Material | Platinum |
| Catalyst Loading | 0.63 Kg/m3 |
| Lifetime | 2-3 Years |
| Density | 0.55 G/cm3 |
|---|---|
| Shelf Life | 2 Years |
| Solubility | Insoluble In Water |
| Storage | Store In A Cool, Dry Place |
| Purity | ≥ 98% |
| Pore Size | 0.3-0.5 Nm |
|---|---|
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Size | 1-3mm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Shape | Granular/spherical |
| Catalyst Life | 2-3 Years |
|---|---|
| Application | Hydrogenation Of Cracked Gasoline |
| Shape | Granular/spherical |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Pore Size | 0.3-0.5 Nm |
| Bulk Density | 0.7-0.9 G/cm3 |
|---|---|
| Shape | Granular/spherical |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Size | 1-3mm |
| Pore Size | 0.3-0.5 Nm |
| Pore Size | 0.3-0.5 Nm |
|---|---|
| Shape | Granular/spherical |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Bulk Density | 0.7-0.9 G/cm3 |
| Catalyst Life | 2-3 Years |