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Overhead vapor Feed 39.2°F, 150 psia 1 Ibmol/h 0.22 59.51 73.57 153.22 173.22 58.22 33.63 N2 150 psia C2 Сз пС4 пC5 пСв Bottoms 99.33 Ibmol/h

Overhead vapor Feed 39.2°F, 150 psia 1 Ibmol/h 0.22 59.51 73.57 153.22 173.22 58.22 33.63 N2 150 psia C2 Сз пС4 пC5 пСв Bottoms 99.33 Ibmol/h

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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Calculate the product compositions, stage temperatures, interstage flow rates and compositions, and reboiler duty for the reboiled stripper shown in Figure.

Overhead vapor Feed 39.2°F, 150 psia 1 Ibmol/h 0.22 59.51 73.57 153.22 173.22 58.22 33.63 N2 150 psia C2 Сз пС4 пC5 пСв Bottoms 99.33 Ibmol/h
Transcribed Image Text:Overhead vapor Feed 39.2°F, 150 psia 1 Ibmol/h 0.22 59.51 73.57 153.22 173.22 58.22 33.63 N2 150 psia C2 Сз пС4 пC5 пСв Bottoms 99.33 Ibmol/h
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