Example 3.1. One thousand (1,000) kilograms of a mixture of benzene (B) and toluene (T), c 40% by mass of B is to be separated into t wo streams in a distillation column. The top outp of the column contains 375 kg of B and the botto m output stream contains 515 kg of T. (a) Perform the mass balance for B & T (b) Determine the composition of the top and bottom streams

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
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Example 3.1. One thousand (1,000) kilograms of a mixture of benzene (B) and toluene (T), containing
40% by mass of B is to be separated into t wo streams in a distillation column. The top output stream
of the column contains 375 kg of B and the bottom output stream contains 515 kg of T.
(a) Perform th e mass balance for B & T
(b) Determine the composition of the top and bottom streams
Transcribed Image Text:Example 3.1. One thousand (1,000) kilograms of a mixture of benzene (B) and toluene (T), containing 40% by mass of B is to be separated into t wo streams in a distillation column. The top output stream of the column contains 375 kg of B and the bottom output stream contains 515 kg of T. (a) Perform th e mass balance for B & T (b) Determine the composition of the top and bottom streams
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