Pore Size | 0.3-0.5 Nm |
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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 |
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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 |
Density | 0.55 G/cm3 |
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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 |
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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 |
Reusability | Yes |
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Support Material | Alumina |
Operating Temperature | 60-100°C |
Selectivity | 80% |
Surface Area | 150-200 M2/g |
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 |
Active Metal | Palladium |
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Particle Size | 3-4.5 Mm |
Industry | Chemical Industry |
Pressure | 3.5MPa |
Support Material | Alumina |
Density | 0.55 G/cm3 |
---|---|
Solubility | Insoluble In Water |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Storage | Store In Dry Place |
Purity | ≥ 98% |