D16.* 10.0 kmol of a 40.0 mol% methanol and 60.0 mol% water mixture is processed in a normal batch distillation system with a still pot that acts as an equilibrium stage and a column with two equilibrium stages (total of three equilibrium contacts). The column has a total condenser, and reflux is a saturated liquid. The column is operated with a varying reflux ratio so that xp is held constant. We desire a final still pot concentration of 8.0 mol% methanol, and distillate should be 84.0 mol% methanol. Pressure is 1 atm, and CMO is valid. a. What initial external reflux ratio, Lo/D, must be used? b. What final external reflux ratio must be used? c. How much distillate product is withdrawn, and what is the value of W final?

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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D16.* 10.0 kmol of a 40.0 mol % methanol and 60.0 mol% water
mixture is processed in a normal batch distillation system with a
still pot that acts as an equilibrium stage and a column with two
equilibrium stages (total of three equilibrium contacts). The
column has a total condenser, and reflux is a saturated liquid. The
column is operated with a varying reflux ratio so that xp is held
constant. We desire a final still pot concentration of 8.0 mol%
methanol, and distillate should be 84.0 mol% methanol. Pressure
is 1 atm, and CMO is valid.
a. What initial external reflux ratio, L₁/D, must be used?
b.
What final external reflux ratio must be used?
c.
How much distillate product is withdrawn, and what is the
value of W final?
Transcribed Image Text:D16.* 10.0 kmol of a 40.0 mol % methanol and 60.0 mol% water mixture is processed in a normal batch distillation system with a still pot that acts as an equilibrium stage and a column with two equilibrium stages (total of three equilibrium contacts). The column has a total condenser, and reflux is a saturated liquid. The column is operated with a varying reflux ratio so that xp is held constant. We desire a final still pot concentration of 8.0 mol% methanol, and distillate should be 84.0 mol% methanol. Pressure is 1 atm, and CMO is valid. a. What initial external reflux ratio, L₁/D, must be used? b. What final external reflux ratio must be used? c. How much distillate product is withdrawn, and what is the value of W final?
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