| Surface Area | 100-110m2/g |
|---|---|
| Shape | Sphere |
| Chemical Composition | Al2O3 ≥ 97% |
| Bulk Density | 0.6-0.7g/cm3 |
| Advantages | High Activity, Good Selectivity, Long Service Life |
| Advantages | High Activity, Good Selectivity, Long Service Life |
|---|---|
| Shape | Sphere |
| Chemical Composition | Al2O3 ≥ 97% |
| Color | White |
| Particle Size | 1.6-1.8mm |
| Cao Content | ≤0.05% |
|---|---|
| Sio2 Content | ≤0.05% |
| Particle Size | 1.6-1.8mm |
| Na2O Content | ≤0.2% |
| Bulk Density | 0.6-0.65 G/cm3 |
| Catalytic Activity | High Selectivity And Conversion Rate |
|---|---|
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
| Pore Volume | 0.8-1.2 Cm3/g |
| Moisture Content | Less Than 1% |
| Thermal Stability | Up To 1000°C |
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
|---|---|
| Bulk Density | 0.3-0.4 G/cm3 |
| Surface Area | 150-170 M2/g |
| Pore Size | 10-15nm |
| Alumina Content | More Than 99% |
| Particle Size | 2 Mm |
|---|---|
| Surface Hydroxyl Groups | High Concentration Of Surface Hydroxyl Groups |
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
| Pore Volume | 0.8-1.2 Cm3/g |
| Bulk Density | 0.3-0.4 G/cm3 |
| Thermal Stability | Up To 1200℃ |
|---|---|
| Na2O Content | ≤0.2% |
| Appearance | White Powder |
| Mgo Content | ≤0.05% |
| Cao Content | ≤0.05% |
| Moisture Content | ≤1% |
|---|---|
| Mgo Content | ≤0.05% |
| Crystalline Phase | Q-Al2O3 |
| Surface Area | 100-110 M2/g |
| Appearance | White Powder |
| Na2O Content | ≤0.2% |
|---|---|
| Fe2O3 Content | ≤0.02% |
| Particle Size | 1.6-1.8mm |
| Appearance | White Powder |
| Cao Content | ≤0.05% |
| Applications | Essential For The Dehydrogenation Of Propane, A Key Process In Producing Propylene Within The Petrochemical Sector. |
|---|---|
| Purity | High Purity |
| Temperature Resistance | High Temperature Resistance |
| Chemical Composition | Al2O3 |
| MgO Content | ≤ 0.05% |