Pore Diameter | 30-80 Å |
---|---|
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 |
---|---|
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 |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Bulk Density | 0.65-0.75 G/cm3 |
---|---|
Hydrogenation Selectivity | ≥ 95% |
Operating Temperature | 150-250°C |
Particle Size | 1.5-3.0 Mm |
Surface Area | ≥ 150 M2/g |
Operating Pressure | 1-10 MPa |
---|---|
Surface Area | ≥ 150 M2/g |
Active Component Loading | ≥ 2 Wt% |
Pore Volume | ≥ 0.35 ML/g |
Support Material Content | ≥ 90 Wt% |
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 |
Particle Size | 2.2-2.6mm |
---|---|
Specific Surface Area | ≥850 M2/g |
Purity | ≥99% |
Carrier Material | Alumina |
Boiling Point | Not Available |
Shape | Spherical |
---|---|
Size | 1-3 Mm |
Bulk Density | 0.7-0.9 G/cm3 |
Pore Size | 0.3-0.5 Nm |
Surface Area | 150-200 M2/g |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
---|---|
Bulk Density | 0.7-0.9 G/cm3 |
Application | Hydrogenation Of Cracked Gasoline |
Reaction Selectivity | 95-98% |
Size | 1-3 Mm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Bulk Density | 0.7-0.9 G/cm3 |
Size | 1-3 Mm |
Reaction Selectivity | 95-98% |