| Fe2O3 Content | ≤0.02% |
|---|---|
| Chemical Formula | Al2O3 |
| Pore Volume | 0.6-0.8 Cm3/g |
| Surface Area | 100-110 M2/g |
| Sio2 Content | ≤0.05% |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
|---|---|
| Purity | ≥ 98% |
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Shelf Life | 2 Years |
| Product Type | Solid Catalyst |
|---|---|
| Heat Stability | High |
| Size | 1.6-1.8 Mm |
| Pore Volume | 0.58-0.66 Cm3/g |
| Shape | Spherical |
| Alumina Content | More Than 99% |
|---|---|
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
| Bulk Density | 0.3-0.4 G/cm3 |
| Thermal Stability | Up To 1000°C |
| Catalytic Activity | High Selectivity And Conversion Rate |
| Carrier Material | Alumina |
|---|---|
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation |
| Specific Surface Area | ≥850 M2/g |
| Boiling Point | Not Available |
| Purity | ≥99% |
| Application | Catalyst Support |
|---|---|
| Product Name | Choose PDH Alumina Carrier For Optimal Performance In High-Temperature And High-Pressure Conditions |
| Packing Density | 0.7-0.9g/cm3 |
| Size | Customizable |
| Applications | Essential For The Dehydrogenation Of Propane, A Key Process In Producing Propylene Within The Petrochemical Sector. |
| Solubility | Insoluble In Water |
|---|---|
| Purity | ≥99% |
| Particle Size | 2.2-2.6mm |
| Carrier Material | Alumina |
| Specific Surface Area | ≥850 M2/g |
| Particle Size | 2.2-2.6mm |
|---|---|
| Specific Surface Area | ≥850 M2/g |
| Purity | ≥99% |
| Carrier Material | Alumina |
| Boiling Point | Not Available |
| Particle Size | 2 Mm |
|---|---|
| Alumina Content | More Than 99% |
| Pore Size | 10-15nm |
| Thermal Stability | Up To 1000°C |
| Catalytic Activity | High Selectivity And Conversion Rate |
| Particle Size | 2 Mm |
|---|---|
| Surface Hydroxyl Groups | High Concentration Of Surface Hydroxyl Groups |
| Surface Area | 150-170 M2/g |
| Thermal Stability | Up To 1000°C |
| Alumina Content | More Than 99% |