Operating Pressure | 1-10 MPa |
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Pore Volume | ≥ 0.35 ML/g |
Pore Diameter | 30-80 Å |
Appearance | Gray Or Black Cylindrical Particles |
Particle Size | 1.5-3.0 Mm |
Support Material | Alumina |
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Active Metal | Palladium |
Operating Temperature | 60-100°C |
Shape | Spherical |
Particle Size | 3-4.5 Mm |
Selectivity | 80% |
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Support Material | Alumina |
Surface Area | 150-200 M2/g |
Active Metal | Palladium |
Application | Selective Hydrogenation Of C2 |
Support Material | Alumina |
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Pressure | 3.5MPa |
Industry | Chemical Industry |
Surface Area | 150-200 M2/g |
Shape | Spherical |
Lifetime | 3-4 Years |
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Size | 1.6 Mm |
Bulk Density | 0.62 G/cm3 |
Pore Size | 20 Nm |
Material | Platinum |
Lifetime | 3-4 Years |
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Product Type | Catalyst |
Shape | Pellet |
Surface Area | 100 M2/g |
Size | 1.6 Mm |
Bulk Density | 0.65-0.75 G/cm3 |
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Catalyst Lifespan | ≥ 3 Years |
Surface Area | ≥ 150 M2/g |
Hydrogenation Selectivity | ≥ 95% |
Operating Pressure | 1-10 MPa |
Selectivity | 80% |
---|---|
Surface Area | 150-200 M2/g |
Reusability | Yes |
Industry | Chemical Industry |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
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Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Reaction Selectivity | 95-98% |
Bulk Density | 0.7-0.9 G/cm3 |
Industry | Chemical Industry |
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Pressure | 3.5MPa |
Active Metal | Palladium |
Reusability | Yes |
Selectivity | 80% |