| Support Material | Aluminum Oxide (Al2O3) |
|---|---|
| Stability | Excellent Stability Under Harsh Conditions |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Catalyst Type | Supported Metal Catalyst |
| Particle Size | Narrow Particle Size Distribution |
| Catalyst Type | Supported Metal Catalyst |
|---|---|
| Shape | Spherical |
| Activity | High Activity For C3 Hydrogenation |
| Stability | Excellent Stability Under Harsh Conditions |
| Pore Size | Uniform Pore Size Distribution |
| Shape | Spherical |
|---|---|
| Pore Size | Uniform Pore Size Distribution |
| Selectivity | High Selectivity C3 Hydrogenation |
| Active Metal | Palladium (Pd) |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |
| Selectivity | 80% |
|---|---|
| Particle Size | 3-4.5 Mm |
| Pore Volume | 0.85-0.95 Cm3/g |
| Surface Area | 150-200 M2/g |
| Shape | Spherical |
| Operating Temperature | 150-250°C |
|---|---|
| Appearance | Gray Or Black Cylindrical Particles |
| Pore Diameter | 30-80 Å |
| Pore Volume | ≥ 0.35 ML/g |
| Particle Size | 1.5-3.0 Mm |
| Shelf Life | 2 Years |
|---|---|
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Solubility | Insoluble In Water |
| Density | 1.25 G/cm3 |
|---|---|
| Solubility | Insoluble In Water |
| Storage | Store In A Cool, Dry Place |
| Purity | ≥ 98% |
| Shelf Life | 2 Years |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
|---|---|
| Pore Volume | 0.3-0.5 Cm3/g |
| Surface Area | 100-200 M2/g |
| Active Component | Palladium (Pd) |
| Appearance | Dark Gray To Black Solid |
| 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 |