Composition | Nickel, Cobalt, Molybdenum, Alumina |
---|---|
Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Pore Size | 0.3-0.5 Nm |
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% |
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 |
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 |
Surface Area | 150-200 M2/g |
---|---|
Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Bulk Density | 0.7-0.9 G/cm3 |
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 |
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) |
Pore Size | 0.3-0.5 Nm |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Reaction Selectivity | 95-98% |
Bulk Density | 0.7-0.9 G/cm3 |
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 |
Operating Temperature | 150-250°C |
---|---|
Shape | Spherical |
Activity | >90% |
Pore Size | 8-12 Nm |
Pore Volume | 0.3-0.5 ML/g |