| Application | Selective Hydrogenation Of C2 |
|---|---|
| Industry | Chemical Industry |
| Shape | Spherical |
| Support Material | Alumina |
| Operating Temperature | 60-100°C |
| Support Material | Alumina Or Silica-alumina |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Bulk Density | 0.65-0.75 G/cm3 |
| Support Material Content | ≥ 90 Wt% |
| Hydrogenation Selectivity | ≥ 95% |
| Density | 0.55 G/cm3 |
|---|---|
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Solubility | Insoluble In Water |
| Shelf Life | 2 Years |
| Purity | ≥ 98% |
| Pore Size | 0.3-0.5 Nm |
|---|---|
| Surface Area | 150-200 M2/g |
| Composition | Nickel, Cobalt, Molybdenum, Alumina |
| Bulk Density | 0.7-0.9 G/cm3 |
| Reaction Selectivity | 95-98% |
| Shape | Spherical |
|---|---|
| Surface Area | 150-200 M2/g |
| Pore Volume | 0.85-0.95 Cm3/g |
| Selectivity | 80% |
| Industry | Chemical Industry |
| Surface Area | ≥ 150 M2/g |
|---|---|
| Support Material Content | ≥ 90 Wt% |
| Active Component | Pd, Pt, Ni, Or Co |
| Hydrogenation Selectivity | ≥ 95% |
| Operating Pressure | 1-10 MPa |
| Density | 0.55 G/cm3 |
|---|---|
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Purity | ≥ 98% |
| Storage | Store In Dry Place |
| Shelf Life | 2 Years |
| Pore Size | 0.3-0.5 Nm |
|---|---|
| Application | Hydrogenation Of Cracked Gasoline |
| Shape | Spherical |
| Reaction Selectivity | 95-98% |
| Bulk Density | 0.7-0.9 G/cm3 |
| Purity | ≥ 98% |
|---|---|
| Solubility | Insoluble In Water |
| Shelf Life | 2 Years |
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
|---|---|
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Shelf Life | 2 Years |
| Solubility | Insoluble In Water |