Shape | Grey Brown Clover |
---|---|
Material | Alumina |
Chemical Composition | Al2O3 |
Regenerability | Good |
Application | C3 Hydrogenation Catalyst For MAPD Removal |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
---|---|
Pore Volume | 0.3-0.5 Cm3/g |
Surface Area | 100-200 M2/g |
Active Component | Palladium (Pd) |
Appearance | Dark Gray To Black Solid |
Catalyst Lifespan | ≥ 3 Years |
---|---|
Active Component | Pd, Pt, Ni, Or Co |
Particle Size | 1.5-3.0 Mm |
Hydrogenation Selectivity | ≥ 95% |
Pore Volume | ≥ 0.35 ML/g |
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% |
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 |
Surface Area | 100-200 M2/g |
---|---|
Promoter | Aluminum Oxide (Al2O3) |
Appearance | Dark Gray To Black Solid |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
Particle Size | 1-3 Mm |
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 |
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 |
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 |
Particle Size | 1-3 Mm |
---|---|
Appearance | Dark Gray To Black Solid |
Surface Area | 100-200 M2/g |
Active Component | Palladium (Pd) |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |