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A vapor mixture of 100 mol/s comprising 55 mol% benzene and 45 mol% toluene is sent to a partial condenser operating at 760 mm Hg. 75 mol % of the toluene in the feed is recovered in the liquid product. Determine all unknown flow rates, compositions, and required heat removal. and do a degree a. Draw a process flow diagram of freedom analysis b. Write out equations used to solve specifications used in Excel Solver unknown flow rates, compositions, and to calculate all C. Specify the temperature and pressure of the feed as T₁ = 102°C and P = 760 mm Hg. Choose the lowest F F enthalpy stream (liquid product stream) for a reference condition. Calculate the required heat removal analytically by hand (No Excel Solver). d. Create Enthalpy Table

A vapor mixture of 100 mol/s comprising 55 mol% benzene and 45 mol% toluene is sent to a partial condenser operating at 760 mm Hg. 75 mol % of the toluene in the feed is recovered in the liquid product. Determine all unknown flow rates, compositions, and required heat removal. and do a degree a. Draw a process flow diagram of freedom analysis b. Write out equations used to solve specifications used in Excel Solver unknown flow rates, compositions, and to calculate all C. Specify the temperature and pressure of the feed as T₁ = 102°C and P = 760 mm Hg. Choose the lowest F F enthalpy stream (liquid product stream) for a reference condition. Calculate the required heat removal analytically by hand (No Excel Solver). d. Create Enthalpy Table

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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Parts c and d please!

HB(feed vapor) = 31.11 kJ/mol

HT (feed vapor) = 35.55 kJ/mol

HB (product vapor) = 30.17 kJ/mol

HT (product vapor) =34.38 kJ/mol

Calculate the heat removed by the process using the energy balance equation.

Q = Ans: -2,172 kJ/s

 

Please show every step you used to solve each problem. A vapor mixture of 100 mol/s comprising 55 mol% benzene and 45 mol % toluene is sent to a partial condenser operating at 760 mm Hg. 75 mol% of the toluene in the feed is recovered in the liquid product. Determine all unknown flow rates, compositions, and required heat removal. and do a degree a. Draw a process flow diagram of freedom analysis b. Write out equations used to solve and to calculate all specifications used in Excel Solver unknown flow rates, compositions, C. F Specify the temperature and pressure of the feed as T₁ = 102°C and P₁ = 760 mm Hg. Choose the lowest enthalpy stream (liquid product stream) for a reference condition. Calculate the required heat removal analytically by hand (No Excel Solver). d. Create Enthalpy Table
Transcribed Image Text:Please show every step you used to solve each problem. A vapor mixture of 100 mol/s comprising 55 mol% benzene and 45 mol % toluene is sent to a partial condenser operating at 760 mm Hg. 75 mol% of the toluene in the feed is recovered in the liquid product. Determine all unknown flow rates, compositions, and required heat removal. and do a degree a. Draw a process flow diagram of freedom analysis b. Write out equations used to solve and to calculate all specifications used in Excel Solver unknown flow rates, compositions, C. F Specify the temperature and pressure of the feed as T₁ = 102°C and P₁ = 760 mm Hg. Choose the lowest enthalpy stream (liquid product stream) for a reference condition. Calculate the required heat removal analytically by hand (No Excel Solver). d. Create Enthalpy Table
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