QUESTIONS No. 8) – 13): The isothermal, irreversible, aqueous phase reaction, A + B - E at 100°F with k = 15- obeys the elementary rate law. Using 1000 ft? Ibmole-hr 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 Ibmole ? GMBE as a function of concentration? a) -r = vo[Cao = Ca)%] b) -7, = ["/v]SE, [C] 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) c) -r, = EAN.[dN,] b) t =; c) w = kCA [kXN Aol
QUESTIONS No. 8) – 13): The isothermal, irreversible, aqueous phase reaction, A + B - E at 100°F with k = 15- obeys the elementary rate law. Using 1000 ft? Ibmole-hr 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 Ibmole ? GMBE as a function of concentration? a) -r = vo[Cao = Ca)%] b) -7, = ["/v]SE, [C] 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) c) -r, = EAN.[dN,] b) t =; c) w = kCA [kXN Aol
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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Please answer numbers 11 and 13. Thank you in advance!
![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](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F4220efb7-607a-41f9-828b-a5715733ff16%2Fa5879757-d6fa-4c43-b091-ecb53b73c003%2Fy8ktxj_processed.png&w=3840&q=75)
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
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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