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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Pore Size | 0.3-0.5 Nm |
Reaction Selectivity | 95-98% |
Application | Hydrogenation Of Cracked Gasoline |
Size | 1-3 Mm |
Surface Area | 150-200 M2/g |
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Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Particle Size | 1-3 Mm |
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Appearance | Dark Gray To Black Solid |
Surface Area | 100-200 M2/g |
Active Component | Palladium (Pd) |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
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 |
Operating Temperature | 150-250°C |
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Appearance | Gray Or Black Cylindrical Particles |
Pore Diameter | 30-80 Å |
Pore Volume | ≥ 0.35 ML/g |
Particle Size | 1.5-3.0 Mm |
Pore Volume | 0.3-0.5 Cm3/g |
---|---|
Particle Size | 1-3 Mm |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
Regenerability | Good |
Thermal Stability | High |
Active Component | Palladium (Pd) |
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Promoter | Aluminum Oxide (Al2O3) |
Appearance | Blue Granule |
Regenerability | Good |
Particle Size | 1-3 Mm |
Active Component | Palladium (Pd) |
---|---|
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
Appearance | Dark Gray To Black Solid |
Pore Volume | 0.3-0.5 Cm3/g |
Promoter | Aluminum Oxide (Al2O3) |
Appearance | Gray Or Black Cylindrical Particles |
---|---|
Operating Temperature | 150-250°C |
Hydrogenation Selectivity | ≥ 95% |
Catalyst Lifespan | ≥ 3 Years |
Active Component Loading | ≥ 2 Wt% |