Chemical Stability | Acid And Alkali Resistant |
---|---|
Shape | Sphere |
Pore Size | 8-015nm |
Thermal Stability | ≥570℃ |
Crushing Strength | ≥40N |
Particle Size | 3-4.5 Mm |
---|---|
Support Material | Alumina |
Shape | Spherical |
Pressure | 3.5MPa |
Industry | Chemical Industry |
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 |
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 |
Selectivity | 80% |
---|---|
Support Material | Alumina |
Surface Area | 150-200 M2/g |
Active Metal | Palladium |
Application | Selective Hydrogenation Of C2 |
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 |
Shape | Spherical |
---|---|
Heat Stability | High |
Product Type | Solid Catalyst |
Lifespan | 4-5 Years |
Size | 1.6-1.8 Mm |
Surface Area | 190-200 M2/g |
---|---|
Product Type | Solid Catalyst |
Size | 1.6-1.8 Mm |
Heat Stability | High |
Lifespan | 4-5 Years |
Shape | Spherical |
---|---|
Pore Volume | 0.58-0.66 Cm3/g |
Lifespan | 4-5 Years |
Size | 1.6-1.8 Mm |
Heat Stability | High |