Feed stream CAO? gmole L-¹ YAO = 0.5 Vo = 6L*s-1 nowns: CAO H V = V = ? L XA = T = 422.2 K P = 10 atm Product stream 0.00596(1-XA) 0.94671 Fao = Caovo TA = FAOXA CAoVOXA (−ra)_exit →V = 0.00596(1 – Xa)0.94671 0.5 10atm L. atm mol.k mol L УАО Rgas FAO = CAOVO = 0.1443- 0.08206 (422.2k) = 0.144 mol *6= = 0.8659- mol L
Feed stream CAO? gmole L-¹ YAO = 0.5 Vo = 6L*s-1 nowns: CAO H V = V = ? L XA = T = 422.2 K P = 10 atm Product stream 0.00596(1-XA) 0.94671 Fao = Caovo TA = FAOXA CAoVOXA (−ra)_exit →V = 0.00596(1 – Xa)0.94671 0.5 10atm L. atm mol.k mol L УАО Rgas FAO = CAOVO = 0.1443- 0.08206 (422.2k) = 0.144 mol *6= = 0.8659- mol L
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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1.
What Volume (CSTR) is required to obtain 96% for the single reactor process.
not sure if i am in the right direction is X_A 96?
also, CA0 was not given so i used ideal gas to calc that
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