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Feed line 0.9 0.8 0.7 R.O.L 0.6 y 0.5 S.O.L 0.4 0.3 0.2 0.1 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 From the above figure, if the feed to the distillation column (F) is 100 kmol/h, calculate the overhead product (D) and the bottoms (B).

Feed line 0.9 0.8 0.7 R.O.L 0.6 y 0.5 S.O.L 0.4 0.3 0.2 0.1 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 From the above figure, if the feed to the distillation column (F) is 100 kmol/h, calculate the overhead product (D) and the bottoms (B).

Introduction to Chemical Engineering Thermodynamics
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
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Feed line 0.9 0.8 0.7 R.O.L 0.6 y 0.5 S.O.L 0.4 0.3 0.2 0.1 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 From the above figure, if the feed to the distillation column (F) is 100 kmol/h, calculate the overhead product (D) and the bottoms (B).
Transcribed Image Text:Feed line 0.9 0.8 0.7 R.O.L 0.6 y 0.5 S.O.L 0.4 0.3 0.2 0.1 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 From the above figure, if the feed to the distillation column (F) is 100 kmol/h, calculate the overhead product (D) and the bottoms (B).
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