| Catalyst Type | Supported Metal Catalyst |
|---|---|
| Particle Size | Narrow Particle Size Distribution |
| Shape | Spherical |
| Activity | High Activity For C3 Hydrogenation |
| Active Metal | Palladium (Pd) |
| Density | 0.55 G/cm3 |
|---|---|
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Solubility | Insoluble In Water |
| Shelf Life | 2 Years |
| Purity | ≥ 98% |
| 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 |
| Bulk Density | 0.65-0.75 G/cm3 |
|---|---|
| Support Material | Alumina Or Silica-alumina |
| Active Component | Pd, Pt, Ni, Or Co |
| Catalyst Lifespan | ≥ 3 Years |
| Particle Size | 1.5-3.0 Mm |
| 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 |
| Reaction Selectivity | 95-98% |
| 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 |
| Particle Size | 1-3 Mm |
|---|---|
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
| Surface Area | 100-200 M2/g |
| Pore Volume | 0.3-0.5 Cm3/g |
| Promoter | Aluminum Oxide (Al2O3) |
| 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 |
| Purity | ≥99% |
|---|---|
| Density | 0.54 G/cm3 |
| Solubility | Insoluble In Water |
| Specific Surface Area | ≥850 M2/g |
| Carrier Material | Alumina |
| Storage | Store In Dry Place |
|---|---|
| Boiling Point | Not Available |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation |
| Density | 0.54 G/cm3 |
| Particle Size | 2.2-2.6mm |