| Operating Pressure | 1-10 MPa |
|---|---|
| Surface Area | ≥ 150 M2/g |
| Active Component Loading | ≥ 2 Wt% |
| Pore Volume | ≥ 0.35 ML/g |
| Support Material Content | ≥ 90 Wt% |
| Particle Size | 2.2-2.6mm |
|---|---|
| Specific Surface Area | ≥850 M2/g |
| Purity | ≥99% |
| Carrier Material | Alumina |
| Boiling Point | Not Available |
| 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 |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
|---|---|
| Application | Hydrogenation Of Cracked Gasoline |
| Bulk Density | 0.7-0.9 G/cm3 |
| Size | 1-3 Mm |
| Reaction Selectivity | 95-98% |
| 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 |
| Purity | ≥99% |
|---|---|
| Density | 0.54 G/cm3 |
| Solubility | Insoluble In Water |
| Specific Surface Area | ≥850 M2/g |
| Carrier Material | Alumina |
| Solubility | Insoluble In Water |
|---|---|
| Shelf Life | 2 Years |
| Storage | Store In Dry Place |
| Density | 0.55 G/cm3 |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Stability | Long-term |
|---|---|
| Surface Area | 100-200 M2/g |
| Active Component Loading | ≥ 2 Wt% |
| Palladium | 0.28% |
| Temperature Range | 150-250°C |
| Boiling Point | Not Available |
|---|---|
| Density | 0.54 G/cm3 |
| Carrier Material | Alumina |
| Specific Surface Area | ≥850 M2/g |
| Solubility | Insoluble In Water |