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Keywords [ selective hydrogenation ] match 188 products.
0.3% Palladium C3 Hydrogenation Catalyst Al2O3 Chemical Composition For MAPD Removal

0.3% Palladium C3 Hydrogenation Catalyst Al2O3 Chemical Composition For MAPD Removal

MOQ: 1T
Shape Grey Brown Clover
Material Alumina
Chemical Composition Al2O3
Regenerability Good
Application C3 Hydrogenation Catalyst For MAPD Removal
Al2O3 Catalyst Used In Hydrogenation Process C8/C9 Palladium Based Catalyst Alumina

Al2O3 Catalyst Used In Hydrogenation Process C8/C9 Palladium Based Catalyst Alumina

MOQ: 1T
Shape Drab Brown Clover
Material Alumina
Chemical Composition Al2O3
Regenerability Good
Application Front-hydrogenation/post-hydrogenation
Reaction Selectivity Cracked Gasoline Hydrogenation Catalyst Spherical Shape 150M2/g-200M2/g

Reaction Selectivity Cracked Gasoline Hydrogenation Catalyst Spherical Shape 150M2/g-200M2/g

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%
Cracked Gasoline h2 catalyst With Excellent Reaction Selectivity 0.3 Nm-0.5 Nm

Cracked Gasoline h2 catalyst With Excellent Reaction Selectivity 0.3 Nm-0.5 Nm

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
30-80 \u00c5 Pores Pd/Pt/Ni Powder Hydrogenation Catalysts Withstand 1-10 MPa Pressure

30-80 \u00c5 Pores Pd/Pt/Ni Powder Hydrogenation Catalysts Withstand 1-10 MPa Pressure

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
Surface Area 150-200 M2/g Cracked Gasoline Hydrogenation Catalyst with 95-98% Reaction Selectivity

Surface Area 150-200 M2/g Cracked Gasoline Hydrogenation Catalyst with 95-98% Reaction Selectivity

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
Long Life Spherical 150-200 M2/G Nickel Based H2 Catalyst / Hydrogenation Catalyst For Refineries

Long Life Spherical 150-200 M2/G Nickel Based H2 Catalyst / Hydrogenation Catalyst For Refineries

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
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
0.65-0.75 G/Cm3 Bulk Density C4/C5 Hydrogenation Process Catalyst Activated At Within Your Budget

0.65-0.75 G/Cm3 Bulk Density C4/C5 Hydrogenation Process Catalyst Activated At Within Your Budget

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
Spherical Surface Area Hydrogenation Catalyst H2 For Cracked Gasoline Processing

Spherical Surface Area Hydrogenation Catalyst H2 For Cracked Gasoline Processing

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
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