| Reaction Selectivity | 95-98% |
|---|---|
| Pore Size | 0.3-0.5 Nm |
| Catalyst Life | 2-3 Years |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Bulk Density | 0.7-0.9 G/cm3 |
| Surface Area | 100-200 M2/g |
|---|---|
| Active Component | Palladium (Pd) |
| Pore Volume | 0.3-0.5 Cm3/g |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
| Particle Size | 1-3 Mm |
| Surface Area | 100-200 M2/g |
|---|---|
| Appearance | Dark Gray To Black Solid |
| Active Component | Palladium (Pd) |
| Pore Volume | 0.3-0.5 Cm3/g |
| Promoter | Aluminum Oxide (Al2O3) |
| Purity | ≥99% |
|---|---|
| Density | 0.54 G/cm3 |
| Solubility | Insoluble In Water |
| Specific Surface Area | ≥850 M2/g |
| Carrier Material | Alumina |
| 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 |
| Surface Area | 100-200 M2/g |
|---|---|
| Appearance | Blue Granule |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
| Active Component | Palladium (Pd) |
| Thermal Stability | High |
| Support Material | Alumina Or Silica-alumina |
|---|---|
| Catalyst Lifespan | ≥ 3 Years |
| Pore Diameter | 30-80 Å |
| Pore Volume | ≥ 0.35 ML/g |
| Active Component | Pd, Pt, Ni, Or Co |
| Support Material | Alumina Or Silica-alumina |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Bulk Density | 0.65-0.75 G/cm3 |
| Support Material Content | ≥ 90 Wt% |
| Hydrogenation Selectivity | ≥ 95% |
| Surface Area | 150-170 M2/g |
|---|---|
| Catalytic Activity | High Selectivity And Conversion Rate |
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
| Moisture Content | Less Than 1% |
| Bulk Density | 0.3-0.4 G/cm3 |