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2) A liquid mixture containing 25 mole% methanol (M), 30 mole% butanol (B), and octylene (0) is fed to a distillation column. The bottoms product containing 97 mole% O and the balance M, and 95% of the O in the feed is recovered in this stream. The overhead product is fed to a second column. The overhead product from the second column contains 95.7 % of the B in the feed to this column. The composition of this stream is 93 mole% of B and no O. Calculate: i. the percentage of the butanol in the process feed (the feed to the first column) that emerges in the overhead product from the second column. i. the percentage of methanol in the process feed that emerges in the bottom product from the second column. 100 mol/h Column Column 93 mole% B 25 mole% (M). 30 mole% (B) 1 97 mole% O 自昆 三 100%

2) A liquid mixture containing 25 mole% methanol (M), 30 mole% butanol (B), and octylene (0) is fed to a distillation column. The bottoms product containing 97 mole% O and the balance M, and 95% of the O in the feed is recovered in this stream. The overhead product is fed to a second column. The overhead product from the second column contains 95.7 % of the B in the feed to this column. The composition of this stream is 93 mole% of B and no O. Calculate: i. the percentage of the butanol in the process feed (the feed to the first column) that emerges in the overhead product from the second column. i. the percentage of methanol in the process feed that emerges in the bottom product from the second column. 100 mol/h Column Column 93 mole% B 25 mole% (M). 30 mole% (B) 1 97 mole% O 自昆 三 100%

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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2) A liquid mixture containing 25 mole% methanol (M), 30 mole% butanol (B), and octylene (0) is fed to a distillation column. The bottoms product containing 97 mole% O and the balance M, and 95% of the O in the feed is recovered in this stream. The overhead product is fed to a second column. The overhead product from the second column contains 95.7 % of the B in the feed to this column. The composition of this stream is 93 mole% of B and no O. Calculate: i. the percentage of the butanol in the process feed (the feed to the first column) that emerges in the overhead product from the second column. i. the percentage of methanol in the process feed that emerges in the bottom product from the second column. 100 mol/h Column Column 93 mole% B 25 mole% (M). 30 mole% (B) 1 97 mole% O 自昆 三 100%
Transcribed Image Text:2) A liquid mixture containing 25 mole% methanol (M), 30 mole% butanol (B), and octylene (0) is fed to a distillation column. The bottoms product containing 97 mole% O and the balance M, and 95% of the O in the feed is recovered in this stream. The overhead product is fed to a second column. The overhead product from the second column contains 95.7 % of the B in the feed to this column. The composition of this stream is 93 mole% of B and no O. Calculate: i. the percentage of the butanol in the process feed (the feed to the first column) that emerges in the overhead product from the second column. i. the percentage of methanol in the process feed that emerges in the bottom product from the second column. 100 mol/h Column Column 93 mole% B 25 mole% (M). 30 mole% (B) 1 97 mole% O 自昆 三 100%
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