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 |
Reaction Selectivity | 95-98% |
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 |
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 |
---|---|
Application | Hydrogenation Of Cracked Gasoline |
Bulk Density | 0.7-0.9 G/cm3 |
Size | 1-3 Mm |
Reaction Selectivity | 95-98% |
Size | 1-3 Mm |
---|---|
Reaction Selectivity | 95-98% |
Pore Size | 0.3-0.5 Nm |
Catalyst Life | 2-3 Years |
Application | Hydrogenation Of Cracked Gasoline |
Shape | Spherical |
---|---|
Pore Size | 0.3-0.5 Nm |
Composition | Nickel, Cobalt, Molybdenum, Alumina |
Reaction Selectivity | 95-98% |
Size | 1-3 Mm |
Surface Area | 150-200 M2/g |
---|---|
Reaction Selectivity | 95-98% |
Shape | Spherical |
Size | 1-3 Mm |
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 |
Size | 1-3 Mm |
---|---|
Reaction Selectivity | 95-98% |
Shape | Spherical |
Pore Size | 0.3-0.5 Nm |
Bulk Density | 0.7-0.9 G/cm3 |
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 |