Bulk Density | 0.7-0.9 G/cm3 |
---|---|
Size | 1-3mm |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Shape | Granular/spherical |
Application | Selective Hydrogenation Of C3 Hydrocarbons |
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Particle Size | Narrow Particle Size Distribution |
Catalyst Type | Supported Metal Catalyst |
Selectivity | High Selectivity C3 Hydrogenation |
Support Material | Aluminum Oxide (Al2O3) |
Pore Size | 0.3-0.5 Nm |
---|---|
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Size | 1-3mm |
Bulk Density | 0.7-0.9 G/cm3 |
Shape | Granular/spherical |
Catalyst Type | Supported Metal Catalyst |
---|---|
Particle Size | Narrow Particle Size Distribution |
Shape | Spherical |
Activity | High Activity For C3 Hydrogenation |
Active Metal | Palladium (Pd) |
Shape | Spherical |
---|---|
Surface Area | 150-200 M2/g |
Pore Volume | 0.85-0.95 Cm3/g |
Selectivity | 80% |
Industry | Chemical Industry |
Support Material | Alumina |
---|---|
Pressure | 3.5MPa |
Industry | Chemical Industry |
Surface Area | 150-200 M2/g |
Shape | Spherical |
Application | Selective Hydrogenation Of C2 |
---|---|
Industry | Chemical Industry |
Shape | Spherical |
Support Material | Alumina |
Operating Temperature | 60-100°C |
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% |
Surface Area | 150-200 M2/g |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Shape | Spherical |
---|---|
Pore Size | Uniform Pore Size Distribution |
Activity | High Activity For C3 Hydrogenation |
Surface Area | High Surface Area For Efficient Catalytic Activity |
Application | Selective Hydrogenation Of C3 Hydrocarbons |