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Modelling of a trickle-bed reactor—the hydrogenation of xylose to xylitol

✍ Scribed by M. Herskowitz


Publisher
Elsevier Science
Year
1985
Tongue
English
Weight
295 KB
Volume
40
Category
Article
ISSN
0009-2509

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The hydrogenation of the main components of an anthracene oil has been investigated in a cocurrent downÑow trickle bed reactor at 623 K and 9É8 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