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We are recovering pyridine from water using chlorobenzene as the solvent in a countercurrent extractor. The feed is 3 5 wt % pyridine and 6
We are recovering pyridine from water using chlorobenzene as the solvent in a countercurrent extractor. The feed is wt pyridine and wt water. Feed flow rate is The solvent used is pure. The desired outlet extract is pyridine, and the desired outlet raffinate is pyridine. Operation is at and atm. Equilibrium data are available in the textbook.
a Find the number of equilibrium stages needed.
b Determine the solvent flow rate required in
The equilibrium for acetic acid extraction from heptanol into water at is where is the weight fraction of acetic acid in water and is the weight fraction of acetic acid in heptanol. We have a feed with that is frac acetic acid and frac heptanol. This feed is contacted in a countercurrent extractor with a solvent that is frac acetic acid and frac water. We desire an outlet raffinate concentration of frac acetic acid and wt frac heptanol. Assume water and heptanol are immiscible and that and are constant.
a If solvent flow rate calculate the exiting extract wt frac and determine the number of equilibrium stages required.
b What are the minimum solvent flow rate and the maximum exiting extract wt fraction.
c This question and Question in the IETutorial" are for the same system, but in one problem and in the other problem. Explain why.
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