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Component K at 100°F, 200 psia C2 2.7 Сз 0.95 C4 0.34 Vapor distillate cw Total 100 °F distillate Component mole fraction C2 Сз Cд 0.10 0.20 0.70 1.00 Liquid distillate

Component K at 100°F, 200 psia C2 2.7 Сз 0.95 C4 0.34 Vapor distillate cw Total 100 °F distillate Component mole fraction C2 Сз Cд 0.10 0.20 0.70 1.00 Liquid distillate

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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Figure shows the overhead system for a distillation column.The composition of the total distillates is indicated, with 10 mol% being vapor. Determine reflux-drum pressure if the temperature is100oF. Use the K-values, assuming that K is inversely proportional to pressure.

Component K at 100°F, 200 psia C2 2.7 Сз 0.95 C4 0.34
Transcribed Image Text:Component K at 100°F, 200 psia C2 2.7 Сз 0.95 C4 0.34
Vapor distillate cw Total 100 °F distillate Component mole fraction C2 Сз Cд 0.10 0.20 0.70 1.00 Liquid distillate
Transcribed Image Text:Vapor distillate cw Total 100 °F distillate Component mole fraction C2 Сз Cд 0.10 0.20 0.70 1.00 Liquid distillate
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