Instead of using a trickle bed reactor for ethanol oxidation (see previous problem), let us consider using

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Instead of using a trickle bed reactor for ethanol oxidation (see previous problem), let us consider using a slurry reactor.

For this type of unit

(kAgai) g+1 = 0.052 s-, dp = 10 +m, f = 0.05, KA4 x fi= 0.75, 10-4 m/s f= 0.2

Take all flows and other values from the previous problem, and then find the expected fractional conversion of ethanol in this reactor.

Data from previous problem

Dilute aqueous ethanol (about 2-3%) is oxidized to acetic acid by the action of pure oxygen at 10 atm in a trickle bed reactor packed with palladium-alumina catalyst pellets and kept at 30°C. According to Sato et al., Proc. First Pacific Chem. Eng. Congress, Kyoto, p. 197,1972, the reaction proceeds as follows:with rate on catalyst O(gl) + CHCHOH(1) CHCOOH(1) + HO (A) (B) - ra = k'CA, k' = 1.77 x 10-5 m/kg-s

Find the fractional conversion of ethanol to acetic acid if gas and liquid are fed to the top of a reactor in the following system:

Gas stream: Liquid stream: Reactor: Catalyst: Kinetics: Ug = 0.01 m/s, H = 86 000 Pa m/mol v = 2 x 10-4 m/s,

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