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Keywords [ selective hydrogenation catalyst ] match 189 Products.
Aluminum Oxide Promoted Hydrogen Palladium Catalyst For Phenylacetylene Hydrogenation

Aluminum Oxide Promoted Hydrogen Palladium Catalyst For Phenylacetylene Hydrogenation

Surface Area 100-200 M2/g
Particle Size 1-3 Mm
Active Component Palladium (Pd)
Application Selective Hydrogenation Of C8/C9 Hydrocarbons
Promoter Aluminum Oxide (Al2O3)
Promoted Dark Gray C9 Pd Al2o3 Catalyst With Surface Area 100-200 M2/G For Hydrogenation

Promoted Dark Gray C9 Pd Al2o3 Catalyst With Surface Area 100-200 M2/G For Hydrogenation

Particle Size 1-3 Mm
Application Selective Hydrogenation Of C8/C9 Hydrocarbons
Surface Area 100-200 M2/g
Pore Volume 0.3-0.5 Cm3/g
Promoter Aluminum Oxide (Al2O3)
Active Component Palladium Pd Catalyst with 100Sqm/g-200Sqm/g Surface Area

Active Component Palladium Pd Catalyst with 100Sqm/g-200Sqm/g Surface Area

Application Selective Hydrogenation Of C8/C9 Hydrocarbons
Particle Size 1-3 Mm
Appearance Dark Gray To Black Solid
Promoter Aluminum Oxide (Al2O3)
Active Component Palladium (Pd)
Spherical Nickel Cobalt Catalyst Cobalt Molybdenum Catalyst With 95-98% Reaction Selectivity 0.7-0.9 Bulk Density

Spherical Nickel Cobalt Catalyst Cobalt Molybdenum Catalyst With 95-98% Reaction Selectivity 0.7-0.9 Bulk Density

Catalyst Life 2-3 Years
Bulk Density 0.7-0.9 G/cm3
Application Hydrogenation Of Cracked Gasoline
Pore Size 0.3-0.5 Nm
Size 1-3 Mm
Highly Active Pt Catalyst For API Production Catalyst Physical Therapy 1.5-3.0 Mm

Highly Active Pt Catalyst For API Production Catalyst Physical Therapy 1.5-3.0 Mm

Active Component Pd, Pt, Ni, Or Co
Particle Size 1.5-3.0 Mm
Support Material Alumina Or Silica-alumina
Active Component Loading ≥ 2 Wt%
Operating Temperature 150-250°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
Alumina Or Silica-Alumina Support Material Content ≥ 90 Wt% C4/C5 For Industrial Applications

Alumina Or Silica-Alumina Support Material Content ≥ 90 Wt% C4/C5 For Industrial Applications

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%
High Pore Volume ≥ 0.35 ML/G Alkyne To Recover Butene Gray Or Black Cylindrical Particles

High Pore Volume ≥ 0.35 ML/G Alkyne To Recover Butene Gray Or Black Cylindrical Particles

Catalyst Lifespan ≥ 3 Years
Operating Temperature 150-250°C
Hydrogenation Selectivity ≥ 95%
Particle Size 1.5-3.0 Mm
Pore Volume ≥ 0.35 ML/g
Temperature C4 C5 Catalyst H2 For Hydrogenation Gray / Black Cylindrical With 30-80A Pore Diameter

Temperature C4 C5 Catalyst H2 For Hydrogenation Gray / Black Cylindrical With 30-80A Pore Diameter

Operating Pressure 1-10 MPa
Pore Volume ≥ 0.35 ML/g
Pore Diameter 30-80 Å
Appearance Gray Or Black Cylindrical Particles
Particle Size 1.5-3.0 Mm
Activity C4/C5 Hydrogenation H2 Catalyst With Gray Or Black Spheres

Activity C4/C5 Hydrogenation H2 Catalyst With Gray Or Black Spheres

Catalyst Lifespan ≥ 3 Years
Appearance Gray Or Black Cylindrical Particles
Operating Pressure 1-10 MPa
Particle Size 1.5-3.0 Mm
Active Component Pd, Pt, Ni, Or Co
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