Pore Diameter | 30-80 Å |
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Operating Pressure | 1-10 MPa |
Active Component Loading | ≥ 2 Wt% |
Support Material | Alumina Or Silica-alumina |
Pore Volume | ≥ 0.35 ML/g |
Density | 0.55 G/cm3 |
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Shelf Life | 2 Years |
Storage | Store In Dry Place |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Solubility | Insoluble In Water |
Selectivity | 80% |
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Surface Area | 150-200 M2/g |
Reusability | Yes |
Industry | Chemical Industry |
Shape | Spherical |
Application | Selective Hydrogenation Of C2 |
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Industry | Chemical Industry |
Shape | Spherical |
Support Material | Alumina |
Operating Temperature | 60-100°C |
Support Material | Alumina Or Silica-alumina |
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Pore Volume | ≥ 0.35 ML/g |
Bulk Density | 0.65-0.75 G/cm3 |
Support Material Content | ≥ 90 Wt% |
Hydrogenation Selectivity | ≥ 95% |
Catalyst Life | 2-3 Years |
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Reaction Selectivity | 95-98% |
Application | Hydrogenation Of Cracked Gasoline |
Pore Size | 0.3-0.5 Nm |
Bulk Density | 0.7-0.9 G/cm3 |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
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Density | 0.55 G/cm3 |
Storage | Store In Dry Place |
Shelf Life | 2 Years |
Solubility | Insoluble In Water |
Catalyst Life | 2-3 Years |
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Pore Size | 0.3-0.5 Nm |
Reaction Selectivity | 95-98% |
Application | Hydrogenation Of Cracked Gasoline |
Size | 1-3 Mm |
Storage | Store In Dry Place |
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Purity | ≥ 98% |
Shelf Life | 2 Years |
Application | Catalyst For 2-ethylanthraquinone Hydrogenation Reactions |
Solubility | Insoluble In Water |
Surface Area | 150-200 M2/g |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |