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C: 0.516 Cy:0.484 100 Ib-moles/h G: 0.352 Cu: 0.648 G: 0.300 Cy: 0.700 C: 0.146 Cu:0.854

C: 0.516 Cy:0.484 100 Ib-moles/h G: 0.352 Cu: 0.648 G: 0.300 Cy: 0.700 C: 0.146 Cu:0.854

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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6. A feed stream containing C8 and C10 hydrocarbons is split into 3 product streams: an overhead fraction, a middle cut and a bottom fraction, whose mole fraction compositions are shown below. Seventy per cent of the C8 entering the column in the feed is recovered in the overhead. On the basis of 100 lb-moles/h of feed determine the molar flow rates of the 3 product streams. Cg: 0.516 Cyo: 0.484 C: 0.352 Co: 0.648 100 Ib-moles/h Cg: 0.300 Cp: 0.700 G: 0.146 Co: 0.854
Transcribed Image Text:6. A feed stream containing C8 and C10 hydrocarbons is split into 3 product streams: an overhead fraction, a middle cut and a bottom fraction, whose mole fraction compositions are shown below. Seventy per cent of the C8 entering the column in the feed is recovered in the overhead. On the basis of 100 lb-moles/h of feed determine the molar flow rates of the 3 product streams. Cg: 0.516 Cyo: 0.484 C: 0.352 Co: 0.648 100 Ib-moles/h Cg: 0.300 Cp: 0.700 G: 0.146 Co: 0.854
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