Operating Temperature | 150-250°C |
---|---|
Appearance | Gray Or Black Cylindrical Particles |
Pore Diameter | 30-80 Å |
Pore Volume | ≥ 0.35 ML/g |
Particle Size | 1.5-3.0 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) |
Surface Area | 150-200 M2/g |
---|---|
Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
Bulk Density | 0.7-0.9 G/cm3 |
Catalyst Life | 2-3 Years |
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Reaction Selectivity | 95-98% |
Application | Hydrogenation Of Cracked Gasoline |
Pore Size | 0.3-0.5 Nm |
Bulk Density | 0.7-0.9 G/cm3 |
Surface Area | 150-200 M2/g |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Surface Area | 100-200 M2/g |
---|---|
Active Component | Palladium (Pd) |
Pore Volume | 0.3-0.5 Cm3/g |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
Particle Size | 1-3 Mm |
Surface Area | 100-200 M2/g |
---|---|
Appearance | Dark Gray To Black Solid |
Active Component | Palladium (Pd) |
Pore Volume | 0.3-0.5 Cm3/g |
Promoter | Aluminum Oxide (Al2O3) |
Promoter | Aluminum Oxide (Al2O3) |
---|---|
Active Component | Palladium (Pd) |
Application | Selective Hydrogenation Of C8/C9 Hydrocarbons |
Surface Area | 100-200 M2/g |
Pore Volume | 0.3-0.5 Cm3/g |
Support Material Content | ≥ 90 Wt% |
---|---|
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% |
---|---|
Active Component | Pd, Pt, Ni, Or Co |
Hydrogenation Selectivity | ≥ 95% |
Support Material Content | ≥ 90 Wt% |
Operating Temperature | 150-250°C |