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High Pressure Precious Metal Hydrogenation Catalyst / 1-10 MPa h2 catalyst

High Pressure Precious Metal Hydrogenation Catalyst / 1-10 MPa h2 catalyst

Bulk Density 0.65-0.75 G/cm3
Support Material Alumina Or Silica-alumina
Active Component Pd, Pt, Ni, Or Co
Catalyst Lifespan ≥ 3 Years
Particle Size 1.5-3.0 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
Insoluble In Water 2-Ethylanthraquinone Hydrogenation Catalyst With 0.55 G/cm3 Density

Insoluble In Water 2-Ethylanthraquinone Hydrogenation Catalyst With 0.55 G/cm3 Density

Solubility Insoluble In Water
Density 0.55 G/cm3
Application Catalyst For 2-ethylanthraquinone Hydrogenation Reactions
Shelf Life 2 Years
Storage Store In Dry Place
0.55G/cm3 2-Ethylanthraquinone Hydrogenation Catalyst Insoluble In Water Shelf Life 2 Years Density 0.55

0.55G/cm3 2-Ethylanthraquinone Hydrogenation Catalyst Insoluble In Water Shelf Life 2 Years Density 0.55

Density 0.55 G/cm3
Shelf Life 2 Years
Storage Store In Dry Place
Application Catalyst For 2-ethylanthraquinone Hydrogenation Reactions
Solubility Insoluble In Water
1.5-3.0 Mm Gray Or Black Hydrogenation Catalyst With 30-80 Å Pore

1.5-3.0 Mm Gray Or Black Hydrogenation Catalyst With 30-80 Å Pore

Appearance Gray Or Black Cylindrical Particles
Operating Temperature 150-250°C
Hydrogenation Selectivity ≥ 95%
Catalyst Lifespan ≥ 3 Years
Active Component Loading ≥ 2 Wt%
Selective Hydrogenation Catalyst For Chemical Industry With 150-200 M2/G Surface Area

Selective Hydrogenation Catalyst For Chemical Industry With 150-200 M2/G Surface Area

Application Selective Hydrogenation Of C2
Industry Chemical Industry
Shape Spherical
Support Material Alumina
Operating Temperature 60-100°C
Alumina Supported C4/C5 Nickel Hydrogenation Catalyst ≥ 0.35 ML/G Pore Volume

Alumina Supported C4/C5 Nickel Hydrogenation Catalyst ≥ 0.35 ML/G Pore Volume

Support Material Alumina Or Silica-alumina
Pore Volume ≥ 0.35 ML/g
Bulk Density 0.65-0.75 G/cm3
Support Material Content ≥ 90 Wt%
Hydrogenation Selectivity ≥ 95%
Hydrogenation Catalyst 0.55 G/Cm3 Density Insoluble In Water Alkyne H2 Lindlar Catalyst

Hydrogenation Catalyst 0.55 G/Cm3 Density Insoluble In Water Alkyne H2 Lindlar Catalyst

Density 0.55 G/cm3
Application Catalyst For 2-ethylanthraquinone Hydrogenation Reactions
Solubility Insoluble In Water
Shelf Life 2 Years
Purity ≥ 98%
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%
Selectivity Industrial Hydrogenation Catalyst 150M2/g-200M2/g Spherical Palladium Catalyst

Selectivity Industrial Hydrogenation Catalyst 150M2/g-200M2/g Spherical Palladium Catalyst

Shape Spherical
Surface Area 150-200 M2/g
Pore Volume 0.85-0.95 Cm3/g
Selectivity 80%
Industry Chemical Industry
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