Q4/in a two stage process, acetic acid (A)is extracted from water (W) into hexanol (H) in a liquid-liquid extraction vessel and the extract is subsequently separated by distillation. Assume that water is completely insoluble in hexanol. A mixture of 18wt% acetic acid and the balance water is feed to liquid-liquid extraction vessel. Pure hexanol is feed to the column to extracted the acetic acid. The water-rich stream leaving the vessel is 99.5wt% water and the balance acetic acid. The hexanol-rich extract from the vessel is feed to a distillation column. The composition of the distillate is 96wt% acetic acid and the balance hexanol. The bottom stream contains 97.2wt% hexanol and recovers 95% of the hexanol feed to the liquid-liquid extraction vessel. Calculate the percentage of acetic acid in the process feed that is recovered in the distillate stream. Distillation Liq-liq Column Extraction

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Q4/in a two stage process, acetic acid (A)is extracted from water (W) into hexanol (H)
in a liquid-liquid extraction vessel and the extract is subsequently separated by distillation.
Assume that water is completely insoluble in hexanol. A mixture of 18wt% acetic acid and
the balance water is feed to liquid-liquid extraction vessel. Pure hexanol is feed to the
column to extracted the acetic acid. The water-rich stream leaving the vessel is 99.5wt%
water and the balance acetic acid. The hexanol-rich extract from the vessel is feed to a
distillation column. The composition of the distillate is 96wt% acetic acid and the balance
hexanol. The bottom stream contains 97.2wt% hexanol and recovers 95% of the hexanol
feed to the liquid-liquid extraction vessel. Calculate the percentage of acetic acid in the
process feed that is recovered in the distillate stream.
Distillation
Liq-liq
Column
Extraction
Transcribed Image Text:Q4/in a two stage process, acetic acid (A)is extracted from water (W) into hexanol (H) in a liquid-liquid extraction vessel and the extract is subsequently separated by distillation. Assume that water is completely insoluble in hexanol. A mixture of 18wt% acetic acid and the balance water is feed to liquid-liquid extraction vessel. Pure hexanol is feed to the column to extracted the acetic acid. The water-rich stream leaving the vessel is 99.5wt% water and the balance acetic acid. The hexanol-rich extract from the vessel is feed to a distillation column. The composition of the distillate is 96wt% acetic acid and the balance hexanol. The bottom stream contains 97.2wt% hexanol and recovers 95% of the hexanol feed to the liquid-liquid extraction vessel. Calculate the percentage of acetic acid in the process feed that is recovered in the distillate stream. Distillation Liq-liq Column Extraction
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