| Composition | Nickel, Cobalt, Molybdenum, Alumina |
|---|---|
| Application | Hydrogenation Of Cracked Gasoline |
| Bulk Density | 0.7-0.9 G/cm3 |
| Size | 1-3 Mm |
| Reaction Selectivity | 95-98% |
| Active Component Loading | ≥ 2 Wt% |
|---|---|
| Pore Volume | ≥ 0.35 ML/g |
| Active Component | Pd, Pt, Ni, Or Co |
| Pore Diameter | 30-80 Å |
| Support Material Content | ≥ 90 Wt% |
| 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 |
| 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 |
| Shape | Spherical |
|---|---|
| Pore Size | Uniform Pore Size Distribution |
| Activity | High Activity For C3 Hydrogenation |
| Surface Area | High Surface Area For Efficient Catalytic Activity |
| Application | Selective Hydrogenation Of C3 Hydrocarbons |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
|---|---|
| Shelf Life | 2 Years |
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Purity | ≥ 98% |
| Solubility | Insoluble In Water |
|---|---|
| Purity | ≥ 98% |
| Storage | Store In Dry Place |
| Shelf Life | 2 Years |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
|---|---|
| Purity | ≥ 98% |
| Density | 0.55 G/cm3 |
| Storage | Store In Dry Place |
| Solubility | Insoluble In Water |
| Active Component | Palladium (Pd) |
|---|---|
| Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
| Appearance | Dark Gray To Black Solid |
| Pore Volume | 0.3-0.5 Cm3/g |
| Promoter | Aluminum Oxide (Al2O3) |
| Density | 0.55 G/cm3 |
|---|---|
| Purity | ≥ 98% |
| Shelf Life | 2 Years |
| Storage | Store In Dry Place |
| Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |