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 |
Support Material | Alumina Or Silica-alumina |
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Catalyst Lifespan | ≥ 3 Years |
Pore Diameter | 30-80 Å |
Pore Volume | ≥ 0.35 ML/g |
Active Component | Pd, Pt, Ni, Or Co |
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 |
Appearance | Gray Or Black Cylindrical Particles |
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Operating Temperature | 150-250°C |
Hydrogenation Selectivity | ≥ 95% |
Catalyst Lifespan | ≥ 3 Years |
Active Component Loading | ≥ 2 Wt% |
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% |
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% |
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 |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
---|---|
Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Pore Size | 0.3-0.5 Nm |
Density | 0.55 G/cm3 |
---|---|
Solubility | Insoluble In Water |
Purity | ≥ 98% |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Storage | Store In Dry Place |