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PDH Alumina Catalyst Carrier Substrate Spheres With Surface Area 100-110M2/G

PDH Alumina Catalyst Carrier Substrate Spheres With Surface Area 100-110M2/G

Crystalline Phase Q-Al2O3
Fe2O3 Content ≤0.02%
Particle Size 1.6-1.8mm
Pore Volume 0.6-0.8 Cm3/g
Moisture Content ≤1%
Large Pore Revolutionize Catalysts PDH Alumina Carrier Ultimate Solution Spherical

Large Pore Revolutionize Catalysts PDH Alumina Carrier Ultimate Solution Spherical

Pore Volume 0.6-0.8 Cm3/g
Na2O Content ≤0.2%
Surface Area 100-110 M2/g
Crystalline Phase Q-Al2O3
Moisture Content ≤1%
100-110 M2/G Oil Refining PDH Alumina Catalyst Carrier With Thermal Stability Up To 1200C

100-110 M2/G Oil Refining PDH Alumina Catalyst Carrier With Thermal Stability Up To 1200C

Cao Content ≤0.05%
Sio2 Content ≤0.05%
Particle Size 1.6-1.8mm
Na2O Content ≤0.2%
Bulk Density 0.6-0.65 G/cm3
PDH Alumina Carrier Optimal Choice For Catalyst Support In Industrial

PDH Alumina Carrier Optimal Choice For Catalyst Support In Industrial

Bulk Density 0.6-0.65 G/cm3
Mgo Content ≤0.05%
Thermal Stability Up To 1200℃
Moisture Content ≤1%
Particle Size 1.6-1.8mm
Experience High Performance Hydrogenation With 2 Ethylanthraquinone Hydrogenation Alumina Carrier

Experience High Performance Hydrogenation With 2 Ethylanthraquinone Hydrogenation Alumina Carrier

Particle Size 2.2-2.6mm
Specific Surface Area ≥850 M2/g
Purity ≥99%
Carrier Material Alumina
Boiling Point Not Available
Heat Stability Solid Oil Column Ccr Alumina Carrier Spherical With 1.6-1.8 Mm Spherical Shape

Heat Stability Solid Oil Column Ccr Alumina Carrier Spherical With 1.6-1.8 Mm Spherical Shape

Product Type Solid Catalyst
Heat Stability High
Size 1.6-1.8 Mm
Pore Volume 0.58-0.66 Cm3/g
Shape Spherical
Insoluble Drip Ball Facilitating Efficient Hydrogenation Reactions Category

Insoluble Drip Ball Facilitating Efficient Hydrogenation Reactions Category

Application Catalyst For 2-ethylanthraquinone Hydrogenation Reactions
Purity ≥ 98%
Density 0.55 G/cm3
Storage Store In Dry Place
Shelf Life 2 Years
Chemical Industry Post Hydrogenation 150-200 M2/g Surface Area Enhanced Productivity And Efficiency

Chemical Industry Post Hydrogenation 150-200 M2/g Surface Area Enhanced Productivity And Efficiency

Shape Spherical
Pressure 3.5MPa
Application Selective Hydrogenation Of C2
Operating Temperature 60-100°C
Selectivity 80%
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
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