Surface Area | 150-200 M2/g |
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Industry | Chemical Industry |
Pressure | 3.5MPa |
Selectivity | 80% |
Application | Selective Hydrogenation Of C2 |
Support Material Content | ≥ 90 Wt% |
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Active Component | Pd, Pt, Ni, Or Co |
Appearance | Gray Or Black Cylindrical Particles |
Pore Diameter | 30-80 Å |
Hydrogenation Selectivity | ≥ 95% |
Active Component Loading | ≥ 2 Wt% |
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Active Component | Pd, Pt, Ni, Or Co |
Hydrogenation Selectivity | ≥ 95% |
Support Material Content | ≥ 90 Wt% |
Operating Temperature | 150-250°C |
Shape | Spherical |
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Lifetime | 3-4 Years |
Catalyst Loading | 0.63 Kg/m3 |
Product Type | Catalyst |
Material | Platinum |
Operating Temperature | 550-650°C |
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Product Type | Catalyst |
Material | Platinum |
Catalyst Loading | 0.63 Kg/m3 |
Lifetime | 2-3 Years |
Density | 0.55 G/cm3 |
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Shelf Life | 2 Years |
Solubility | Insoluble In Water |
Storage | Store In A Cool, Dry Place |
Purity | ≥ 98% |
Pore Size | 0.3-0.5 Nm |
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Composition | Nickel, Cobalt, Molybdenum, Alumina |
Size | 1-3mm |
Bulk Density | 0.7-0.9 G/cm3 |
Shape | Granular/spherical |
Catalyst Life | 2-3 Years |
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Application | Hydrogenation Of Cracked Gasoline |
Shape | Granular/spherical |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Pore Size | 0.3-0.5 Nm |
Bulk Density | 0.7-0.9 G/cm3 |
---|---|
Shape | Granular/spherical |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Size | 1-3mm |
Pore Size | 0.3-0.5 Nm |
Pore Size | 0.3-0.5 Nm |
---|---|
Shape | Granular/spherical |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Bulk Density | 0.7-0.9 G/cm3 |
Catalyst Life | 2-3 Years |