1. One hundred tons per hour of a feed containing 20 wt% Na2CO3 and the balance insoluble solids is to be leached and washed with water in a continuous, countercurrent system. Assume leaching will be completed in one ideal stage. It is desired to obtain a final extract containing 15 wt% solute, with a 98% recovery of solute. The underflow from each stage will contain 0.5 lb solution/lb insoluble solid. Determine the number of ideal washing stages using both graphical and analytical solutions.

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Author:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
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1. One hundred tons per hour of a feed containing 20
wt% Na2CO3 and the balance insoluble solids is to
be leached and washed with water in a continuous,
countercurrent system. Assume leaching will be
completed in one ideal stage. It is desired to obtain
a final extract containing 15 wt% solute, with a 98%
recovery of solute.
The underflow from each stage will contain 0.5 lb
solution/lb insoluble solid.
Determine the number of ideal washing stages
using both graphical and analytical solutions.
Transcribed Image Text:1. One hundred tons per hour of a feed containing 20 wt% Na2CO3 and the balance insoluble solids is to be leached and washed with water in a continuous, countercurrent system. Assume leaching will be completed in one ideal stage. It is desired to obtain a final extract containing 15 wt% solute, with a 98% recovery of solute. The underflow from each stage will contain 0.5 lb solution/lb insoluble solid. Determine the number of ideal washing stages using both graphical and analytical solutions.
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