Composition | Nickel, Cobalt, Molybdenum, Alumina |
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Application | Hydrogenation Of Cracked Gasoline |
Bulk Density | 0.7-0.9 G/cm3 |
Size | 1-3 Mm |
Reaction Selectivity | 95-98% |
Surface Area | 150-200 M2/g |
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Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Bulk Density | 0.7-0.9 G/cm3 |
Active Component Loading | ≥ 2 Wt% |
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Pore Volume | ≥ 0.35 ML/g |
Active Component | Pd, Pt, Ni, Or Co |
Pore Diameter | 30-80 Å |
Support Material Content | ≥ 90 Wt% |
Solubility | Insoluble In Water |
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Density | 0.55 G/cm3 |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Shelf Life | 2 Years |
Storage | Store In Dry Place |
Density | 0.55 G/cm3 |
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Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Solubility | Insoluble In Water |
Shelf Life | 2 Years |
Purity | ≥ 98% |
Shape | Spherical |
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Surface Area | 150-200 M2/g |
Pore Volume | 0.85-0.95 Cm3/g |
Selectivity | 80% |
Industry | Chemical Industry |
Surface Area | ≥ 150 M2/g |
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Support Material Content | ≥ 90 Wt% |
Active Component | Pd, Pt, Ni, Or Co |
Hydrogenation Selectivity | ≥ 95% |
Operating Pressure | 1-10 MPa |
Industry | Chemical Industry |
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Pressure | 3.5MPa |
Active Metal | Palladium |
Reusability | Yes |
Selectivity | 80% |
Purity | ≥ 98% |
---|---|
Solubility | Insoluble In Water |
Shelf Life | 2 Years |
Density | 0.55 G/cm3 |
Storage | Store In Dry Place |
Shape | Spherical |
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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 |