Operating Pressure | 1-10 MPa |
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Surface Area | ≥ 150 M2/g |
Active Component Loading | ≥ 2 Wt% |
Pore Volume | ≥ 0.35 ML/g |
Support Material Content | ≥ 90 Wt% |
Bulk Density | 0.65-0.75 G/cm3 |
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Support Material | Alumina Or Silica-alumina |
Active Component | Pd, Pt, Ni, Or Co |
Catalyst Lifespan | ≥ 3 Years |
Particle Size | 1.5-3.0 Mm |
Particle Size | 2.2-2.6mm |
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Specific Surface Area | ≥850 M2/g |
Purity | ≥99% |
Carrier Material | Alumina |
Boiling Point | Not Available |
Shape | Spherical |
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Size | 1-3 Mm |
Bulk Density | 0.7-0.9 G/cm3 |
Pore Size | 0.3-0.5 Nm |
Surface Area | 150-200 M2/g |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
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Bulk Density | 0.7-0.9 G/cm3 |
Application | Hydrogenation Of Cracked Gasoline |
Reaction Selectivity | 95-98% |
Size | 1-3 Mm |
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% |
Purity | ≥99% |
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Density | 0.54 G/cm3 |
Solubility | Insoluble In Water |
Specific Surface Area | ≥850 M2/g |
Carrier Material | Alumina |
Stability | Long-term |
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Surface Area | 100-200 M2/g |
Active Component Loading | ≥ 2 Wt% |
Palladium | 0.28% |
Temperature Range | 150-250°C |
Solubility | Insoluble In Water |
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Shelf Life | 2 Years |
Storage | Store In Dry Place |
Density | 0.55 G/cm3 |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Boiling Point | Not Available |
---|---|
Density | 0.54 G/cm3 |
Carrier Material | Alumina |
Specific Surface Area | ≥850 M2/g |
Solubility | Insoluble In Water |