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Keywords [ spherical hydrogenation catalyst ] match 69 products.

Top C2 Selective Hydrogenation Catalyst 80% Selectivity Pore Volume Of 0.85-0.95 Cm3/g On Alumina Support Material

Top C2 Selective Hydrogenation Catalyst 80% Selectivity Pore Volume Of 0.85-0.95 Cm3/g On Alumina Support Material

Surface Area	150-200 M2/g
Industry	Chemical Industry
Pressure	3.5MPa
Selectivity	80%
Application	Selective Hydrogenation Of C2

Cracked Gasoline Hydrogenation Catalyst 2-3 Year Lifespan 0.3-0.5nm Pore

Cracked Gasoline Hydrogenation Catalyst 2-3 Year Lifespan 0.3-0.5nm Pore

Catalyst Life	2-3 Years
Application	Hydrogenation Of Cracked Gasoline
Shape	Granular/spherical
Composition	Nickel, Cobalt, Molybdenum, Alumina
Pore Size	0.3-0.5 Nm

Surface Area C3 Selective Hydrogenation Catalyst with Excellent Stability Supported Metal Catalyst

Surface Area C3 Selective Hydrogenation Catalyst with Excellent Stability Supported Metal Catalyst

Surface Area	High Surface Area For Efficient Catalytic Activity
Pore Size	Uniform Pore Size Distribution
Stability	Excellent Stability Under Harsh Conditions
Particle Size	Narrow Particle Size Distribution
Operating Temperature	30-35°C

Selective C2 Hydrogenation Catalyst With 80% Selectivity For Chemical Industry Reusable And With 0.85-0.95

Selective C2 Hydrogenation Catalyst With 80% Selectivity For Chemical Industry Reusable And With 0.85-0.95

Selectivity	80%
Reusability	Yes
Industry	Chemical Industry
Application	Selective Hydrogenation Of C2
Particle Size	3-4.5 Mm

80% Selectivity Reusable Hydrogenation Catalyst For Chemical Industry

80% Selectivity Reusable Hydrogenation Catalyst For Chemical Industry

Selectivity	80%
Surface Area	150-200 M2/g
Reusability	Yes
Industry	Chemical Industry
Shape	Spherical

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

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

Advanced Nickel Cobalt Molybdenum Nickel Catalyst For Ammonia Cracking Gasoline Hydrogenation Catalyst

Advanced Nickel Cobalt Molybdenum Nickel Catalyst For Ammonia Cracking Gasoline Hydrogenation Catalyst

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%

High Surface Area Alumina Hydrogenation Catalyst Supported Cracked Gasoline 0.3Nm-0.5Nm

High Surface Area Alumina Hydrogenation Catalyst Supported Cracked Gasoline 0.3Nm-0.5Nm

Pore Size	0.3-0.5 Nm
Application	Hydrogenation Of Cracked Gasoline
Shape	Spherical
Reaction Selectivity	95-98%
Bulk Density	0.7-0.9 G/cm3

Excellent Stability Under Harsh Conditions C3 Selective Hydrogenation Catalyst For Extreme Temperatures

Excellent Stability Under Harsh Conditions C3 Selective Hydrogenation Catalyst For Extreme Temperatures

Active Metal	Palladium (Pd)
Particle Size	Narrow Particle Size Distribution
Support Material	Aluminum Oxide (Al2O3)
Activity	High Activity For C3 Hydrogenation
Surface Area	High Surface Area For Efficient Catalytic Activity

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