Active Metal | Palladium |
---|---|
Particle Size | 3-4.5 Mm |
Industry | Chemical Industry |
Pressure | 3.5MPa |
Support Material | Alumina |
Pore Volume | 0.85-0.95 Cm3/g |
---|---|
Shape | Spherical |
Pressure | 3.5MPa |
Selectivity | 80% |
Support Material | Alumina |
Bulk Density | 0.65-0.75 G/cm3 |
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Particle Size | 1.5-3.0 Mm |
Operating Temperature | 150-250°C |
Operating Pressure | 1-10 MPa |
Active Component | Pd, Pt, Ni, Or Co |
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 |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
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Surface Area | 100-200 M2/g |
Appearance | Dark Gray To Black Solid |
Active Component | Palladium (Pd) |
Particle 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% |
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 |
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 |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
---|---|
Appearance | Dark Gray To Black Solid |
Active Component | Palladium (Pd) |
Particle Size | 1-3 Mm |
Pore Volume | 0.3-0.5 Cm3/g |
Catalyst Life | 2-3 Years |
---|---|
Reaction Selectivity | 95-98% |
Application | Hydrogenation Of Cracked Gasoline |
Pore Size | 0.3-0.5 Nm |
Bulk Density | 0.7-0.9 G/cm3 |