Catalyst Type | Supported Metal Catalyst |
---|---|
Selectivity | High Selectivity C3 Hydrogenation |
Support Material | Aluminum Oxide (Al2O3) |
Regenerability | Can Be Regenerated Multiple Times Without Significant Loss Of Activity |
Operating Temperature | 30-35°C |
Reusability | Yes |
---|---|
Pore Volume | 0.85-0.95 Cm3/g |
Support Material | Alumina |
Pressure | 3.5MPa |
Industry | Chemical Industry |
Industry | Chemical Industry |
---|---|
Pressure | 3.5MPa |
Active Metal | Palladium |
Reusability | Yes |
Selectivity | 80% |
Operating Temperature | 150-250°C |
---|---|
Shape | Spherical |
Activity | >90% |
Pore Size | 8-12 Nm |
Pore Volume | 0.3-0.5 ML/g |
Surface Area | 190-200 M2/g |
---|---|
Shape | Spherical |
Size | 1.6-1.8 Mm |
Pore Volume | 0.58-0.66 Cm3/g |
Product Type | Solid Catalyst |
Particle Size | 3-4.5 Mm |
---|---|
Support Material | Alumina |
Shape | Spherical |
Pressure | 3.5MPa |
Industry | Chemical Industry |
Shape | Spherical |
---|---|
Pressure | 3.5MPa |
Application | Selective Hydrogenation Of C2 |
Operating Temperature | 60-100°C |
Selectivity | 80% |
Selectivity | 80% |
---|---|
Support Material | Alumina |
Surface Area | 150-200 M2/g |
Active Metal | Palladium |
Application | Selective Hydrogenation Of C2 |
Pore Size | 15-25nm |
---|---|
Shape | Spherical |
Material | Alumina |
Chemical Composition | Al2O3 |
Regenerability | Good |
Catalyst Life | 2-3 Years |
---|---|
Bulk Density | 0.7-0.9 G/cm3 |
Application | Hydrogenation Of Cracked Gasoline |
Pore Size | 0.3-0.5 Nm |
Size | 1-3 Mm |