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1. Saturated liquid feed of F = 40 mol/hr, containing 50 mol% A(1)/B(2), is supplied to the apparatus as shown. The condensate is split so that molar flow rate ratio of reflux/distillate = 1. If heat is supplied such that W = 30 mol/hr and a = 2 = PA/P at, what will be the composition of the distillate and the bottoms product? Vapor Condenser Still pot Feed Distillate Reflux Heat Bottoms

1. Saturated liquid feed of F = 40 mol/hr, containing 50 mol% A(1)/B(2), is supplied to the apparatus as shown. The condensate is split so that molar flow rate ratio of reflux/distillate = 1. If heat is supplied such that W = 30 mol/hr and a = 2 = PA/P at, what will be the composition of the distillate and the bottoms product? Vapor Condenser Still pot Feed Distillate Reflux Heat Bottoms

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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1. Saturated liquid feed of F = 40 mol/hr, containing 50 mol% A(1)/B(2), is supplied to the apparatus as shown. The condensate is split so that molar flow rate ratio of reflux/distillate = 1. If heat is supplied such that W = 30 mol/hr and a = 2 = PAs/P3, what will be the composition of the distillate and the bottoms product? Vapor Condenser Still pot Feed Distillate Reflux Heat Bottoms
Transcribed Image Text:1. Saturated liquid feed of F = 40 mol/hr, containing 50 mol% A(1)/B(2), is supplied to the apparatus as shown. The condensate is split so that molar flow rate ratio of reflux/distillate = 1. If heat is supplied such that W = 30 mol/hr and a = 2 = PAs/P3, what will be the composition of the distillate and the bottoms product? Vapor Condenser Still pot Feed Distillate Reflux Heat Bottoms
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