| Density | 0.55 G/cm3 |
|---|---|
| Purity | ≥ 98% |
| Shelf Life | 2 Years |
| Storage | Store In Dry Place |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| 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 |
| Particle Size | 2.2-2.6mm |
|---|---|
| Storage | Store In Dry Place |
| Carrier Material | Alumina |
| Purity | ≥99% |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation |
| 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 |
| Catalyst Loading | 0.63 Kg/m3 |
|---|---|
| Product Type | Catalyst |
| Pore Size | 20 Nm |
| Material | Platinum |
| Lifetime | 3-4 Years |
| Application | Petrochemical Industry |
|---|---|
| Product Type | Catalyst |
| Material | Platinum |
| Pore Size | 20 Nm |
| Catalyst Loading | 0.63 Kg/m3 |
| Support Material | Alumina Or Silica-alumina |
|---|---|
| Catalyst Lifespan | ≥ 3 Years |
| Pore Diameter | 30-80 Å |
| Pore Volume | ≥ 0.35 ML/g |
| Active Component | Pd, Pt, Ni, Or Co |
| Pore Diameter | 30-80 Å |
|---|---|
| Operating Pressure | 1-10 MPa |
| Active Component Loading | ≥ 2 Wt% |
| Support Material | Alumina Or Silica-alumina |
| Pore Volume | ≥ 0.35 ML/g |
| Catalyst Life | 2-3 Years |
|---|---|
| Reaction Selectivity | 95-98% |
| Application | Hydrogenation Of Cracked Gasoline |
| Pore Size | 0.3-0.5 Nm |
| Bulk Density | 0.7-0.9 G/cm3 |
| 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 |