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fo de exi & Given data belaw n-Hexane Benzene Join to op VL (em ³ /mol) x 32. 8 (J/cm³) 1/2 14.9 18-8 We are designing distillation extermin, then we weed K factors (ki=7₁) xi, At 50'e a Liquid mixture contains 30 moley.n-hexame and 70 moley. benzene. *00-fra calculate K factors for benzene and n-hexame in this mixture. At 50°C, pure component vapor pressures are 0.533 bar for n-hexane and 0.380 bar for n-benzene, C-A ORTOP Assuming the pressure is much low to neglect corrections and Payuting factors!

fo de exi & Given data belaw n-Hexane Benzene Join to op VL (em ³ /mol) x 32. 8 (J/cm³) 1/2 14.9 18-8 We are designing distillation extermin, then we weed K factors (ki=7₁) xi, At 50'e a Liquid mixture contains 30 moley.n-hexame and 70 moley. benzene. *00-fra calculate K factors for benzene and n-hexame in this mixture. At 50°C, pure component vapor pressures are 0.533 bar for n-hexane and 0.380 bar for n-benzene, C-A ORTOP Assuming the pressure is much low to neglect corrections and Payuting factors!

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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temperature 626.0 Torr 8117 experin ed fo e de e ex] 6.8114 Given data belaw п-нехать Benzene Torr. CALO edomos 2² (em ³ /mol) 132. 8 (J/cm³) 1/2 14.9 18-8 We are designing distillation extermin, then we weed K factors At 50'e a Liquid mixture contains 30 moley.n-hexame and 70 maley. benzene. Calculate K factors for benzene and n-hexame in this mixture. At 50°C, pure component vapor pressures are 0.538 bar for A-hexane and 0.380 bar for n-benzene, 334 OP preks Assuming the pressure is much low to neglect gas phone corrections and Poyuting factors!
Transcribed Image Text:temperature 626.0 Torr 8117 experin ed fo e de e ex] 6.8114 Given data belaw п-нехать Benzene Torr. CALO edomos 2² (em ³ /mol) 132. 8 (J/cm³) 1/2 14.9 18-8 We are designing distillation extermin, then we weed K factors At 50'e a Liquid mixture contains 30 moley.n-hexame and 70 maley. benzene. Calculate K factors for benzene and n-hexame in this mixture. At 50°C, pure component vapor pressures are 0.538 bar for A-hexane and 0.380 bar for n-benzene, 334 OP preks Assuming the pressure is much low to neglect gas phone corrections and Poyuting factors!
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