| Surface Hydroxyl Groups | High Concentration Of Surface Hydroxyl Groups |
|---|---|
| Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
| Moisture Content | Less Than 1% |
| Pore Volume | 0.8-1.2 Cm3/g |
| Surface Area | 150-170 M2/g |
| 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% |
| Abrasion Resistance | Excellent |
|---|---|
| Chemical Resistance | Acids And Bases |
| Material | Alumina |
| Thermal Conductivity | High |
| Pore Size | Medium |
| Description | The PDH Alumina Carrier Is A High-performance Material Known For Its Unique Characteristics And Vital Role In Catalytic Processes. |
|---|---|
| Chemical Stability | Acid And Alkali Resistant |
| Bulk Density | 0.6-0.65 G/cm3 |
| Pore Size | 0.4-0.6nm |
| Applications | Essential For The Dehydrogenation Of Propane, A Key Process In Producing Propylene Within The Petrochemical Sector. |
| Active Metal | Palladium |
|---|---|
| Catalyst Type | Heterogeneous |
| Thermal Stability | High |
| Particle Size | 1-3 Mm |
| Selectivity | >95% |
| Crushing Strength | ≥40N |
|---|---|
| Surface Area | 190-210m2/g |
| Mechanical Strength | High |
| Thermal Stability | ≥570℃ |
| Abrasion Resistance | Excellent |
| Particle Size | 1.6-1.8mm |
|---|---|
| Sio2 Content | ≤0.05% |
| Thermal Stability | Up To 1200℃ |
| Na2O Content | ≤0.2% |
| Bulk Density | 0.6-0.65 G/cm3 |
| Pore Volume | 0.6-0.8 Cm3/g |
|---|---|
| Cao Content | ≤0.05% |
| Na2O Content | ≤0.2% |
| Surface Area | 100-110 M2/g |
| Crystalline Phase | Q-Al2O3 |
| Operating Temperature | 150-250°C |
|---|---|
| Shape | Spherical |
| Activity | >90% |
| Pore Size | 8-12 Nm |
| Pore Volume | 0.3-0.5 ML/g |
| Abrasion Resistance | Excellent |
|---|---|
| Material | Alumina |
| Mechanical Strength | High |
| Water Absorption | Low |
| Surface Area | 200 M2/g |