Lifespan | 4-5 Years |
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Surface Area | 190-200 M2/g |
Product Type | Solid Catalyst |
Heat Stability | High |
Size | 1.6-1.8 Mm |
Application | Petrochemical Industry |
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Product Type | Catalyst |
Material | Platinum |
Pore Size | 20 Nm |
Catalyst Loading | 0.63 Kg/m3 |
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 |
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 |
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 |
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 |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
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Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Pore Size | 0.3-0.5 Nm |
Reaction Selectivity | 95-98% |
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Pore Size | 0.3-0.5 Nm |
Catalyst Life | 2-3 Years |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Bulk Density | 0.7-0.9 G/cm3 |
Stability | Excellent Stability Under Harsh Conditions |
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Operating Temperature | 30-35°C |
Pore Size | Uniform Pore Size Distribution |
Application | Selective Hydrogenation Of C3 Hydrocarbons |
Active Metal | Palladium (Pd) |