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QUESTIONS No. 8) – 13): The isothermal, irreversible, aqueous phase reaction, A + B - E at 100°F with k = 15- stirred tank reactor with a feed a feed of 2000, what will be the outlet concentration of E if the inlet concentration A and B are both 0.25- obeys the elementary rate law. Using 1000 ft Ibmole-hr Ibmole ?

QUESTIONS No. 8) – 13): The isothermal, irreversible, aqueous phase reaction, A + B - E at 100°F with k = 15- stirred tank reactor with a feed a feed of 2000, what will be the outlet concentration of E if the inlet concentration A and B are both 0.25- obeys the elementary rate law. Using 1000 ft Ibmole-hr Ibmole ?

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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QUESTIONS No. 8) – 13): The isothermal, irreversible, aqueous phase reaction, A + B - E at 100°F with k = 15; stirred tank reactor with a feed a feed of 2000 , what will be the outlet concentration of E if the inlet concentration A and B are both 0.25 8) What is the rate equation for a steady state, well mixed CSTR derived from the GMBE as a function of concentration? obeys the elementary rate law. Using 1000 ft lbmole-hr hr lbmole a) -"A = vo[Cao - Ca b) -7, = [/v]SE^ [C) %3D d) -ra = Ao 9) What is the equation derived from the combined mole balance and rate law for a steady state, well-mixed CSTR, as a function of conversion? a) – In (1– x) b) t = c) w = d) [kCAo(1-x) 10)A substitution of the values given in the problems into equation derived from the combined mole balance and rate law for a steady state , well-mixed CSTR, as a function of conversion, results into equation: a) In(1 – x) = 1.875 b) d) In x = 2.875 11) The conversion of the reaction is: a) 0.533 b) 1- 2.5333X + x² = 0 C) 1= 0.533X + x b) 5.52 ) 0.4982 d) 0.1223
Transcribed Image Text:QUESTIONS No. 8) – 13): The isothermal, irreversible, aqueous phase reaction, A + B - E at 100°F with k = 15; stirred tank reactor with a feed a feed of 2000 , what will be the outlet concentration of E if the inlet concentration A and B are both 0.25 8) What is the rate equation for a steady state, well mixed CSTR derived from the GMBE as a function of concentration? obeys the elementary rate law. Using 1000 ft lbmole-hr hr lbmole a) -"A = vo[Cao - Ca b) -7, = [/v]SE^ [C) %3D d) -ra = Ao 9) What is the equation derived from the combined mole balance and rate law for a steady state, well-mixed CSTR, as a function of conversion? a) – In (1– x) b) t = c) w = d) [kCAo(1-x) 10)A substitution of the values given in the problems into equation derived from the combined mole balance and rate law for a steady state , well-mixed CSTR, as a function of conversion, results into equation: a) In(1 – x) = 1.875 b) d) In x = 2.875 11) The conversion of the reaction is: a) 0.533 b) 1- 2.5333X + x² = 0 C) 1= 0.533X + x b) 5.52 ) 0.4982 d) 0.1223
12) The final concentration of E as a function of X is: a) Cg = Cảo(1 – 2x) b) Cg = Cao(1 - X) 13) The final concentration of E is: a) 0.25 lbmole/ft b) 0.117 bmole/ft c) 0.063 lbmole/ft d) 1.38 lbmole/ft c) Cg = XCA0 d) Cg = Cao (1 – X)?
Transcribed Image Text:12) The final concentration of E as a function of X is: a) Cg = Cảo(1 – 2x) b) Cg = Cao(1 - X) 13) The final concentration of E is: a) 0.25 lbmole/ft b) 0.117 bmole/ft c) 0.063 lbmole/ft d) 1.38 lbmole/ft c) Cg = XCA0 d) Cg = Cao (1 – X)?
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