2.3 Kg/s of solid containing 0.55 Kg/s soluble material is to be washed with 2.8 Kg/s pure solvent in a counter – current unit . The final residue is to contain not more than 0.1% solute when dried . Find the number of stages given that the amount of solution in under flow varies with solute concentration according to the relation : W = 0.2 X + 0.3 , Also find the concentration and quantities in and out from each stage .

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
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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2.3 Kg/s of solid containing 0.55 Kg/s soluble material is to be washed with 2.8 Kg/s pure solvent in a counter – current unit . The final residue is to contain not more than 0.1% solute when dried . Find the number of stages given that the amount of solution in under flow varies with solute concentration according to the relation : W = 0.2 X + 0.3 , Also find the concentration and quantities in and out from each stage .

03:- Fresh halibut livers containing 25.7% (weight percent) oil are to
be extracted with pure ethyl ether to remove 95% of the oil in a
counter
current multistage leaching process . The feed rate is 1000 Kg
of the fresh liver per hour . The final exit over flow solution is to be contain
70% by mass oil . The molar flow varies as follows .
16
Mass Transfer
Third Year
Assist. Prof. Dr. Ahmed Daham
Kg solution / kg inert solid
Kg oil / kg solution
0.205
0.286
0.2
0.405
0.4
0.599
0.6
0.719
0.81
Calculate the amount & composition of the exit streams and the total number of
the theoretical stages.
Transcribed Image Text:03:- Fresh halibut livers containing 25.7% (weight percent) oil are to be extracted with pure ethyl ether to remove 95% of the oil in a counter current multistage leaching process . The feed rate is 1000 Kg of the fresh liver per hour . The final exit over flow solution is to be contain 70% by mass oil . The molar flow varies as follows . 16 Mass Transfer Third Year Assist. Prof. Dr. Ahmed Daham Kg solution / kg inert solid Kg oil / kg solution 0.205 0.286 0.2 0.405 0.4 0.599 0.6 0.719 0.81 Calculate the amount & composition of the exit streams and the total number of the theoretical stages.
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