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1000 Kilogram |
FOB Price: USD 4.9600 |
Hydrogenation catalyst catalyst Thiophene conversion rate,% 98
Hydrogenation catalyst for refinery coking dry gas hydrogenation desulfurization and olefin hydrogen plant
Hydrogenation catalyst takes theγ-alumina ball as the carrier,adding active additives,contains molybdenum, cobalt and other active components.The catalyst is mainly used for olefinic or carbon monoxide, carbon dioxide gas, high coke oven gas, water gas hydrogenation conversion,it is especially suitable for refinery coking dry gas hydrogenation desulfurization and olefin hydrogen plant.After hydrogenation organic sulfur is less than 0.05ppm, and the content of olefin is lower than 0.1%.
Hydrogenation catalyst for refinery coking dry gas hydrogenation desulfurization and olefin hydrogen plant
Hydrogenation catalyst takes theγ-alumina ball as the carrier,adding active additives,contains molybdenum, cobalt and other active components.The catalyst is mainly used for olefinic or carbon monoxide, carbon dioxide gas, high coke oven gas, water gas hydrogenation conversion,it is especially suitable for refinery coking dry gas hydrogenation desulfurization and olefin hydrogen plant.After hydrogenation organic sulfur is less than 0.05ppm, and the content of olefin is lower than 0.1%.
Physical and chemical properties:
Appearance |
sphere |
size,mm,∮ |
2-4 |
MoO3 content,%,≥ |
11.0 |
CoO content,%,≥ |
2.5 |
NiO content,% ≥ |
1.5 |
Crushing strength,N/particle,≥ |
50 |
abrasiveness,% ≤ |
1.0 |
Bulk density,kg/L |
0.60-0.70 |
Process condition:
pressure,Mpa |
1.0-6.0 |
temperature,℃ |
200-300 |
Space velocity,hr-1 |
1500 |
Feedstock: |
Inorganic sulfur in the inlet 200-400ppm, olefine≤8.0% |
Product: |
Inorganic sulfur in the outlet<0.05ppm, olefine≤0.1% |
Packing: usually packed in plastic bag, net weight 30Kg.It can also be based on user requirements for packaging.
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