| Size | 1-3 Mm |
|---|---|
| Reaction Selectivity | 95-98% |
| Pore Size | 0.3-0.5 Nm |
| Catalyst Life | 2-3 Years |
| Application | Hydrogenation Of Cracked Gasoline |
| Catalyst Lifespan | ≥ 3 Years |
|---|---|
| Appearance | Gray Or Black Cylindrical Particles |
| Operating Pressure | 1-10 MPa |
| Particle Size | 1.5-3.0 Mm |
| Active Component | Pd, Pt, Ni, Or Co |
| Size | 1-3 Mm |
|---|---|
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
| Pore Size | 0.3-0.5 Nm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Stability | Excellent Stability Under Harsh Conditions |
|---|---|
| Operating Temperature | 30-35°C |
| Pore Size | Uniform Pore Size Distribution |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |
| Active Metal | Palladium (Pd) |
| Operating Pressure | 1-10 MPa |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Pore Diameter | 30-80 Å |
| Appearance | Gray Or Black Cylindrical Particles |
| Particle Size | 1.5-3.0 Mm |
| Surface Area | 150-200 M2/g |
|---|---|
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
| Size | 1-3 Mm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Shape | Drab Brown Clover |
|---|---|
| Material | Alumina |
| Chemical Composition | Al2O3 |
| Regenerability | Good |
| Application | One/two-stage Hydrogenation Of Cracked Gasoline |
| 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% |
