It is intended to absorb benzene from an oil stream through a tower in contact with steam. The inlet oil stream contains 8% moles of benzene and the steam stream is free of benzene. It is desired to recover 80% of benzene using steam at a rate 1.4 times the minimum flow. Clean oil (benzene free, Ls) flows at a rate of 6.94 mols/L/. Determine the amount in moles of steam per second required if: A)A tower with countercurrent supply is used (R= 1.57 lbmol/s) B)A tower with parallel feed is used (R=11.46 lbmol/sec ) x (mol of benzene/mol of oil)   y (mol of benzene/mol of steam)      The Table is attached

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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It is intended to absorb benzene from an oil stream through a tower in contact with steam. The inlet oil stream contains 8% moles of benzene and the steam stream is free of benzene. It is desired to recover 80% of benzene using steam at a rate 1.4 times the minimum flow. Clean oil (benzene free, Ls) flows at a rate of 6.94 mols/L/. Determine the amount in moles of steam per second required if:

A)A tower with countercurrent supply is used (R= 1.57 lbmol/s)

B)A tower with parallel feed is used (R=11.46 lbmol/sec )

x (mol of benzene/mol of oil)   y (mol of benzene/mol of steam)

     The Table is attached

x (mol de benzeno/mol de óleo)
y (mol de benzeno/mol de vapor)
0,02
0,07
0,04
0,14
0,06
0,22
0,08
0,31
0,10
0,405
0,12
0,515
0,14
0,65
Transcribed Image Text:x (mol de benzeno/mol de óleo) y (mol de benzeno/mol de vapor) 0,02 0,07 0,04 0,14 0,06 0,22 0,08 0,31 0,10 0,405 0,12 0,515 0,14 0,65
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