| Pore Volume | 0.85-0.95 Cm3/g |
|---|---|
| Shape | Spherical |
| Pressure | 3.5MPa |
| Selectivity | 80% |
| Support Material | Alumina |
| Shape | Spherical |
|---|---|
| Stability | Excellent Stability Under Harsh Conditions |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Pore Size | Uniform Pore Size Distribution |
| Selectivity | High Selectivity C3 Hydrogenation |
| Bulk Density | 0.65-0.75 G/cm3 |
|---|---|
| Particle Size | 1.5-3.0 Mm |
| Operating Temperature | 150-250°C |
| Operating Pressure | 1-10 MPa |
| Active Component | Pd, Pt, Ni, Or Co |
| Pore Diameter | 30-80 Å |
|---|---|
| Operating Pressure | 1-10 MPa |
| Active Component Loading | ≥ 2 Wt% |
| Support Material | Alumina Or Silica-alumina |
| Pore Volume | ≥ 0.35 ML/g |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
|---|---|
| Surface Area | 100-200 M2/g |
| Appearance | Dark Gray To Black Solid |
| Active Component | Palladium (Pd) |
| Particle 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% |
| Surface Area | ≥ 150 M2/g |
|---|---|
| Support Material Content | ≥ 90 Wt% |
| Active Component | Pd, Pt, Ni, Or Co |
| Hydrogenation Selectivity | ≥ 95% |
| Operating Pressure | 1-10 MPa |
| Lifespan | 4-5 Years |
|---|---|
| Surface Area | 190-200 M2/g |
| Product Type | Solid Catalyst |
| Heat Stability | High |
| Size | 1.6-1.8 Mm |
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
|---|---|
| Appearance | Dark Gray To Black Solid |
| Active Component | Palladium (Pd) |
| Particle Size | 1-3 Mm |
| Pore Volume | 0.3-0.5 Cm3/g |
| Catalyst Life | 2-3 Years |
|---|---|
| Reaction Selectivity | 95-98% |
| Application | Hydrogenation Of Cracked Gasoline |
| Pore Size | 0.3-0.5 Nm |
| Bulk Density | 0.7-0.9 G/cm3 |