Q4) Distillation column (Figure Q4) separates 10000 kg/hr of a 50% benzene-50% toluene mixture. The product (D) recovered from the condenser at the top of the column contains 98% benzene, and the bottom (W) from the column contains 90% toluene. Calculate the mass flowrate of the top and bottom product and calculate the mass and molar fraction of the top and bottom products.

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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100%
Q4) Distillation column (Figure Q4) separates 10000 kg/hr of a
50% benzene-50% toluene mixture. The product (D) recovered
Condensor
from the condenser at the top of the column contains 98%
benzene, and the bottom (W) from the column contains 90%
D
toluene. Calculate the mass flowrate of the top and bottom
product and calculate the mass and molar fraction of the top and
Distillation
bottom products.
Reboiler
Figure: Q4
R.
Transcribed Image Text:Q4) Distillation column (Figure Q4) separates 10000 kg/hr of a 50% benzene-50% toluene mixture. The product (D) recovered Condensor from the condenser at the top of the column contains 98% benzene, and the bottom (W) from the column contains 90% D toluene. Calculate the mass flowrate of the top and bottom product and calculate the mass and molar fraction of the top and Distillation bottom products. Reboiler Figure: Q4 R.
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