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0.90 Exact y, Mole Fraction 0.80 0.70 0.60 0.50 0.40 0.376 0.30 0.20 (0.300, 0.556)

0.90 Exact y, Mole Fraction 0.80 0.70 0.60 0.50 0.40 0.376 0.30 0.20 (0.300, 0.556)

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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Answers:

a) 0.94

b)0.30

c)1.00

d)4.0

e)1.72

1.00 Evaluation 0.90 Exact Ma v. Mole Fraction 0.90 0.70 0.60 0.30 0.40 0.376 0.30 0.20 0,10 0.00 0.00 (0.300, 0.556) 0.10 0.20 0.30 What is the Distillate recovery? [a] What is the Feed mole fraction? [b] What is the q-value? [c] What is the reflux ratio, R? [d] What is the Boil-Up ratio? [e] 0.40 0.50 x, Mole Fraction 0.60 0.70 0.30 0.50 1.00
Transcribed Image Text:1.00 Evaluation 0.90 Exact Ma v. Mole Fraction 0.90 0.70 0.60 0.30 0.40 0.376 0.30 0.20 0,10 0.00 0.00 (0.300, 0.556) 0.10 0.20 0.30 What is the Distillate recovery? [a] What is the Feed mole fraction? [b] What is the q-value? [c] What is the reflux ratio, R? [d] What is the Boil-Up ratio? [e] 0.40 0.50 x, Mole Fraction 0.60 0.70 0.30 0.50 1.00
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