| Particle Size | 1-3 Mm |
|---|---|
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
| Promoter | Aluminum Oxide (Al2O3) |
| Surface Area | 100-200 M2/g |
| Active Component | Palladium (Pd) |
| Support Material | Aluminum Oxide (Al2O3) |
|---|---|
| Particle Size | Narrow Particle Size Distribution |
| Pore Size | Uniform Pore Size Distribution |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |
| Regenerability | Can Be Regenerated Multiple Times Without Significant Loss Of Activity |
| Solubility | Insoluble In Water |
|---|---|
| Purity | ≥ 98% |
| Storage | Store In Dry Place |
| Shelf Life | 2 Years |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| 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 |
| Pore Volume | 0.58-0.66 Cm3/g |
|---|---|
| Heat Stability | High |
| Product Type | Solid Catalyst |
| Lifespan | 4-5 Years |
| Surface Area | 190-200 M2/g |
| Bulk Density | 0.7-0.9 G/cm3 |
|---|---|
| Size | 1-3mm |
| Pore Size | 0.3-0.5 Nm |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Shape | Granular/spherical |
| Operating Temperature | 550-650°C |
|---|---|
| Pore Size | 20 Nm |
| Shape | Pellet |
| Product Type | Catalyst |
| Bulk Density | 0.62 G/cm3 |
| 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 |
| Active Component Loading | ≥ 2 Wt% |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Active Component | Pd, Pt, Ni, Or Co |
| Pore Diameter | 30-80 Å |
| Support Material Content | ≥ 90 Wt% |
| Shape | Spherical |
|---|---|
| Support Material | Aluminum Oxide (Al2O3) |
| Activity | High Activity For C3 Hydrogenation |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Selectivity | High Selectivity C3 Hydrogenation |