Start Specifled feed Specify spilts of two key components Estimate spilts of nonkey components Determine column pressure Bubble-pointidew-point calculations and type of condenser Repeat only If estimated Flash the feed Adlabatic flash procedure at column pressure and calculated spilts of nonkey components differ Calculate minimum Fenske equation theoretical stages Iderably Calculate splits of nonkey components Fenske equation Calculate minimum reflux ratio Underwood equations Calculate actual theoretical stages for specifled reflux ratlo > minimum value GIIland correlation Calculate feed Kirkbride equation stage location Calculate condenser Energy-balance equations and reboller dutles Exit
Start Specifled feed Specify spilts of two key components Estimate spilts of nonkey components Determine column pressure Bubble-pointidew-point calculations and type of condenser Repeat only If estimated Flash the feed Adlabatic flash procedure at column pressure and calculated spilts of nonkey components differ Calculate minimum Fenske equation theoretical stages Iderably Calculate splits of nonkey components Fenske equation Calculate minimum reflux ratio Underwood equations Calculate actual theoretical stages for specifled reflux ratlo > minimum value GIIland correlation Calculate feed Kirkbride equation stage location Calculate condenser Energy-balance equations and reboller dutles Exit
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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A feed of 62 mol% para-dichlorobenzene in ortho-dichlorobenzene is separated by distillation at near-atmospheric pressure into a distillate containing 98 mol% para isomer and bottoms of 96 mol% ortho isomer. If a total condenser and partial reboiler are used, q=0.9, average α = 1.154, and R/Rmin=1.15, use the FUG procedure to estimate the theoretical stages required.
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