160 cm³/s of a solvent S is used to treat 400cm³/s of a 10 per cent by mass solution of A in B, in a three-stage countercurrent multiple-contact liquid-liquid extraction plant. What is the composition of the final raffinate? Using the same total amount of solvent, evenly distributed between the three stages, what would be the composition of the final raffinate if the equipment were used in a simple multiple-contact arrangement? Equilibrium data: kg A/kg B: kg A/kg S: Densities (kg/m³): 0.05 0.069 PA-1200, 0.10 0.159 -1000, 0.15 0.258 Ps - 800

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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Example 13.1
160 cm³/s of a solvent S is used to treat 400cm³/s of a 10 per cent by mass solution of A in B, in a
three-stage countercurrent multiple-contact liquid-liquid extraction plant. What is the composition
of the final raffinate?
Using the same total amount of solvent, evenly distributed between the three stages, what would
be the composition of the final raffinate if the equipment were used in a simple multiple-contact
arrangement?
Equilibrium data:
kg A/kg B:
kg A/kg S:
Densities (kg/m³):
0.05
0.069
PA = 1200,
0.10
0.159
P=1000,
0.15
0.258
Ps= 800
Transcribed Image Text:Example 13.1 160 cm³/s of a solvent S is used to treat 400cm³/s of a 10 per cent by mass solution of A in B, in a three-stage countercurrent multiple-contact liquid-liquid extraction plant. What is the composition of the final raffinate? Using the same total amount of solvent, evenly distributed between the three stages, what would be the composition of the final raffinate if the equipment were used in a simple multiple-contact arrangement? Equilibrium data: kg A/kg B: kg A/kg S: Densities (kg/m³): 0.05 0.069 PA = 1200, 0.10 0.159 P=1000, 0.15 0.258 Ps= 800
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