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Model for pressure drop hysteresis in trickle-beds

✍ Scribed by C. F. Chu; K. M. Ng

Publisher
American Institute of Chemical Engineers
Year
1989
Tongue
English
Weight
472 KB
Volume
35
Category
Article
ISSN
0001-1541

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## Abstract Desulfurization and hydrogenation of aromatics in diesel oil were investigated in an isothermally operated trickle‐bed reactor 500 mm long and with a 19‐mm ID, using commercial bifunctional NiMo/Al~2~O~3~ catalysts. The operating temperature, pressure, liquid hourly space velocity, gas/