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Effect of transport processes on conversion in a trickle-bed reactor

✍ Scribed by Nicholas D. Sylvester; Punya Pitayagulsarn


Publisher
American Institute of Chemical Engineers
Year
1973
Tongue
English
Weight
475 KB
Volume
19
Category
Article
ISSN
0001-1541

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Catalytic hydrogenation of aromatic hydr
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The hydrogenation of the main components of an anthracene oil has been investigated in a cocurrent downΓ‘ow trickle bed reactor at 623 K and 9Γ‰8 MPa. The catalyst employed was sulÐded The product of NiÈMo/c-Al 2 O 3 . the e †ectiveness factor and chemical rate constant was determined for the reactio