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Surface Area Nickel Hydrogenation Catalyst Cracked Gasoline With High Reaction Selectivity

Surface Area Nickel Hydrogenation Catalyst Cracked Gasoline With High Reaction Selectivity

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 Spherical C3 Hydrogenation Catalyst With Excellent Stability

Surface Area Spherical C3 Hydrogenation Catalyst With Excellent Stability

Shape Spherical
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
1-3 Mm Nickel Cobalt Molybdenum Alumina Hydrogenation Catalyst With 150 M2/G-200 M2/G Surface Area

1-3 Mm Nickel Cobalt Molybdenum Alumina Hydrogenation Catalyst With 150 M2/G-200 M2/G Surface Area

Composition Nickel, Cobalt, Molybdenum, Alumina
Reaction Selectivity 95-98%
Shape Spherical
Size 1-3 Mm
Pore Size 0.3-0.5 Nm
150-200 M2/g Palladium Spherical C2 Selective Hydrogenation Catalyst -60-100.C

150-200 M2/g Palladium Spherical C2 Selective Hydrogenation Catalyst -60-100.C

Surface Area 150-200 M2/g
Shape Spherical
Active Metal Palladium
Reusability Yes
Operating Temperature 60-100°C
0.3-0.5 Nm Pores Nickel Catalysts For Long Term Use Nickel Alumina Catalyst

0.3-0.5 Nm Pores Nickel Catalysts For Long Term Use Nickel Alumina Catalyst

Reaction Selectivity 95-98%
Pore Size 0.3-0.5 Nm
Catalyst Life 2-3 Years
Composition Nickel, Cobalt, Molybdenum, Alumina
Bulk Density 0.7-0.9 G/cm3
Excellent Under Harsh Conditions Activity Hydrogenation Catalyst / H2 Catalyst 30-35°C

Excellent Under Harsh Conditions Activity Hydrogenation Catalyst / H2 Catalyst 30-35°C

Stability Excellent Stability Under Harsh Conditions
Operating Temperature 30-35°C
Pore Size Uniform Pore Size Distribution
Application Selective Hydrogenation Of C3 Hydrocarbons
Active Metal Palladium (Pd)
High Selectivity Al2O3 Palladium Pd Catalyst for C3 Hydrogenation Process

High Selectivity Al2O3 Palladium Pd Catalyst for C3 Hydrogenation Process

Catalyst Type Supported Metal Catalyst
Support Material Aluminum Oxide (Al2O3)
Activity High Activity For C3 Hydrogenation
Particle Size Narrow Particle Size Distribution
Application Selective Hydrogenation Of C3 Hydrocarbons
Surface Area Spherical C3 Selective Hydrogenation Catalyst Palladium Pd

Surface Area Spherical C3 Selective Hydrogenation Catalyst Palladium Pd

Shape Spherical
Pore Size Uniform Pore Size Distribution
Activity High Activity For C3 Hydrogenation
Surface Area High Surface Area For Efficient Catalytic Activity
Application Selective Hydrogenation Of C3 Hydrocarbons
High Performance Platinum Based PDH Catalyst With 0.62 G/cm3 Bulk Density For Petrochemical Industries

High Performance Platinum Based PDH Catalyst With 0.62 G/cm3 Bulk Density For Petrochemical Industries

Pore Size 20 Nm
Material Platinum
Size 1.6 Mm
Lifetime 3-4 Years
Shape Pellet
0.63 Kg/m3 Platinum Catalyst For Enhanced 550-650C Distillation

0.63 Kg/m3 Platinum Catalyst For Enhanced 550-650C Distillation

Operating Temperature 550-650°C
Pore Size 20 Nm
Size 1.6 Mm
Lifetime 3-4 Years
Material Platinum
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