| Operating Pressure | 1-10 MPa |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Pore Diameter | 30-80 Å |
| Appearance | Gray Or Black Cylindrical Particles |
| Particle Size | 1.5-3.0 Mm |
| Pore Size | Uniform Pore Size Distribution |
|---|---|
| Regenerability | Can Be Regenerated Multiple Times Without Significant Loss Of Activity |
| Catalyst Type | Supported Metal Catalyst |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Activity | High Activity For C3 Hydrogenation |
| Density | 0.55 G/cm3 |
|---|---|
| Purity | ≥ 98% |
| Shelf Life | 2 Years |
| Solubility | Insoluble In Water |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Surface Area | 150-200 M2/g |
|---|---|
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
| Size | 1-3 Mm |
| Bulk Density | 0.7-0.9 G/cm3 |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
|---|---|
| Purity | ≥ 98% |
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Solubility | Insoluble In Water |
| Storage | Store In Dry Place |
|---|---|
| Solubility | Insoluble In Water |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Purity | ≥ 98% |
| Density | 0.55 G/cm3 |
| 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 |
| Reusability | Yes |
|---|---|
| Support Material | Alumina |
| Operating Temperature | 60-100°C |
| Selectivity | 80% |
| Surface Area | 150-200 M2/g |
| Shape | Drab Brown Clover |
|---|---|
| Material | Alumina |
| Chemical Composition | Al2O3 |
| Regenerability | Good |
| Application | One/two-stage Hydrogenation Of Cracked Gasoline |
| 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 |