Pore Volume | 0.58-0.66 Cm3/g |
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Heat Stability | High |
Product Type | Solid Catalyst |
Lifespan | 4-5 Years |
Surface Area | 190-200 M2/g |
Operating Temperature | 550-650°C |
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Pore Size | 20 Nm |
Shape | Pellet |
Product Type | Catalyst |
Bulk Density | 0.62 G/cm3 |
Catalyst Life | 2-3 Years |
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Bulk Density | 0.7-0.9 G/cm3 |
Application | Hydrogenation Of Cracked Gasoline |
Pore Size | 0.3-0.5 Nm |
Size | 1-3 Mm |
Active Component Loading | ≥ 2 Wt% |
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Pore Volume | ≥ 0.35 ML/g |
Active Component | Pd, Pt, Ni, Or Co |
Pore Diameter | 30-80 Å |
Support Material Content | ≥ 90 Wt% |
Shape | Spherical |
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Support Material | Aluminum Oxide (Al2O3) |
Activity | High Activity For C3 Hydrogenation |
Surface Area | High Surface Area For Efficient Catalytic Activity |
Selectivity | High Selectivity C3 Hydrogenation |
Catalyst Loading | 0.63 Kg/m3 |
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Lifetime | 3-4 Years |
Material | Platinum |
Surface Area | 100 M2/g |
Pore Size | 20 Nm |
Shape | Spherical |
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Stability | Excellent Stability Under Harsh Conditions |
Surface Area | High Surface Area For Efficient Catalytic Activity |
Pore Size | Uniform Pore Size Distribution |
Selectivity | High Selectivity C3 Hydrogenation |
Catalyst Type | Supported Metal Catalyst |
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Support Material | Aluminum Oxide (Al2O3) |
Activity | High Activity For C3 Hydrogenation |
Particle Size | Narrow Particle Size Distribution |
Application | Selective Hydrogenation Of C3 Hydrocarbons |
Particle Size | 1-3 Mm |
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Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
Promoter | Aluminum Oxide (Al2O3) |
Surface Area | 100-200 M2/g |
Active Component | Palladium (Pd) |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
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Particle Size | 1-3 Mm |
Appearance | Dark Gray To Black Solid |
Promoter | Aluminum Oxide (Al2O3) |
Active Component | Palladium (Pd) |