| Surface Hydroxyl Groups | High Concentration Of Surface Hydroxyl Groups |
|---|---|
| Alumina Content | More Than 99% |
| Particle Size | 2 Mm |
| Catalytic Activity | High Selectivity And Conversion Rate |
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
| Color | White |
|---|---|
| Crushing Strength | ≥80N |
| Cao Content | ≤0.05% |
| Chemical Composition | Al2O3 ≥ 97% |
| Size | 1-5mm |
| Bulk Density | 0.62 G/cm3 |
|---|---|
| Surface Area | 100 M2/g |
| Size | 1.6 Mm |
| Operating Temperature | 550-650°C |
| Catalyst Loading | 0.63 Kg/m3 |
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
|---|---|
| Surface Area | 150-170 M2/g |
| Pore Size | 10-15nm |
| Pore Volume | 0.8-1.2 Cm3/g |
| Bulk Density | 0.3-0.4 G/cm3 |
| Pore Volume | 0.8-1.2 Cm3/g |
|---|---|
| Catalytic Activity | High Selectivity And Conversion Rate |
| Bulk Density | 0.3-0.4 G/cm3 |
| Particle Size | 2 Mm |
| Pore Size | 10-15nm |
| 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% |
| 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 |
| Application | Propane Dehydrogenation (PDH) |
|---|---|
| Thermal Stability | ≥900℃ |
| Crushing Strength | ≥45N |
| Shape | Sphere |
| Bulk Density | 0.6-0.7g/cm3 |
| Application | Propane Dehydrogenation (PDH) |
|---|---|
| Advantages | High Activity, Good Selectivity, Long Service Life |
| Bulk Density | 0.6-0.7g/cm3 |
| Crushing Strength | ≥45N |
| Color | White |
| Color | White |
|---|---|
| Crushing Strength | ≥45N |
| Bulk Density | 0.6-0.7g/cm3 |
| Thermal Stability | ≥900℃ |
| Application | Propane Dehydrogenation (PDH) |