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 |
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) |
Industry | Chemical Industry |
---|---|
Support Material | Alumina |
Surface Area | 150-200 M2/g |
Shape | Spherical |
Selectivity | 80% |
Surface Area | High Surface Area For Efficient Catalytic Activity |
---|---|
Pore Size | Uniform Pore Size Distribution |
Stability | Excellent Stability Under Harsh Conditions |
Particle Size | Narrow Particle Size Distribution |
Operating Temperature | 30-35°C |
Support Material | Alumina |
---|---|
Active Metal | Palladium |
Operating Temperature | 60-100°C |
Shape | Spherical |
Particle Size | 3-4.5 Mm |
Application | Selective Hydrogenation Of C2 |
---|---|
Industry | Chemical Industry |
Shape | Spherical |
Support Material | Alumina |
Operating Temperature | 60-100°C |
Surface Area | 150-200 M2/g |
---|---|
Shape | Spherical |
Active Metal | Palladium |
Reusability | Yes |
Operating Temperature | 60-100°C |
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 |
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 |
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 |