k1 → k2 15 pts.) 8) Consider the set of liquid phase, elementary series reactions A B C to be carried out in a 10 L batch reactor. The reaction occurs at 300K, where k₁ = 0.6 h¹ and k₂ = 0.25 h¹. The reaction starts with 4 mol/L pure A. a) Calculate the maximum concentration of B (CBmax) and the time it takes to reach that concentration (tmas). 3 species: A,B,C dt MB: dCA =rA dCB=rb dcc= at at =rc 0.6h1 0.25 0.6h-1 10.25-0.6 10.6)0.25-1 (0.25/tmax= (Bmax (0.1") (0.6h") [_ (0°2017- свтах 0.25h-1 Just need to solve this Ki KI K2-KI K2 K2-Ki (Bmax = RICA (KL)² - (11) K K K2-14 b) Calculate CA, CB, and Cc after 4 hours. -Kit CBmax √o.bah' (0.25h) tmax=2√15 -2 h 3 - KICA 2√ kyk₂ +ki+kz сво CA = Amol/L Pure A = CBo CAOC CA-YA dCB=rb dcc=rc CH dt at YA=KACA -rij=kij f YAYB |- rc = -0.6h (4h) - CA Amol/Le CBA CB = K₁CA | e-Kit - e-k₂t 257 CB = (0.6h) (4ml) e-oh (4)/2 = 10.25 (4) [e-0. e-0.6h-1 0.25-1 CAO [K2 (1-e-kit) - ki(1-e-k₂+), = VB = XC CC = K₂cki ==
k1 → k2 15 pts.) 8) Consider the set of liquid phase, elementary series reactions A B C to be carried out in a 10 L batch reactor. The reaction occurs at 300K, where k₁ = 0.6 h¹ and k₂ = 0.25 h¹. The reaction starts with 4 mol/L pure A. a) Calculate the maximum concentration of B (CBmax) and the time it takes to reach that concentration (tmas). 3 species: A,B,C dt MB: dCA =rA dCB=rb dcc= at at =rc 0.6h1 0.25 0.6h-1 10.25-0.6 10.6)0.25-1 (0.25/tmax= (Bmax (0.1") (0.6h") [_ (0°2017- свтах 0.25h-1 Just need to solve this Ki KI K2-KI K2 K2-Ki (Bmax = RICA (KL)² - (11) K K K2-14 b) Calculate CA, CB, and Cc after 4 hours. -Kit CBmax √o.bah' (0.25h) tmax=2√15 -2 h 3 - KICA 2√ kyk₂ +ki+kz сво CA = Amol/L Pure A = CBo CAOC CA-YA dCB=rb dcc=rc CH dt at YA=KACA -rij=kij f YAYB |- rc = -0.6h (4h) - CA Amol/Le CBA CB = K₁CA | e-Kit - e-k₂t 257 CB = (0.6h) (4ml) e-oh (4)/2 = 10.25 (4) [e-0. e-0.6h-1 0.25-1 CAO [K2 (1-e-kit) - ki(1-e-k₂+), = VB = XC CC = K₂cki ==
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
Related questions
Question
Parts A and B please!!
Transcribed Image Text:k1
→
k2
15 pts.) 8) Consider the set of liquid phase, elementary series reactions A B C to be carried out in a
10 L batch reactor. The reaction occurs at 300K, where k₁ = 0.6 h¹ and k₂ = 0.25 h¹. The
reaction starts with 4 mol/L pure A.
a) Calculate the maximum concentration of B (CBmax) and the time it takes to reach that
concentration (tmas). 3 species: A,B,C
dt
MB: dCA =rA dCB=rb dcc=
at
at
=rc
0.6h1
0.25
0.6h-1 10.25-0.6 10.6)0.25-1
(0.25/tmax=
(Bmax (0.1") (0.6h") [_ (0°2017-
свтах
0.25h-1
Just need to solve this
Ki
KI K2-KI
K2
K2-Ki
(Bmax = RICA (KL)² - (11) K K
K2-14
b) Calculate CA, CB, and Cc after 4 hours.
-Kit
CBmax
√o.bah' (0.25h)
tmax=2√15
-2
h
3
-
KICA
2√ kyk₂ +ki+kz
сво
CA = Amol/L Pure A = CBo
CAOC
CA-YA dCB=rb dcc=rc
CH
dt
at
YA=KACA -rij=kij f
YAYB
|-
rc
=
-0.6h (4h) -
CA Amol/Le
CBA CB = K₁CA | e-Kit - e-k₂t
257
CB = (0.6h) (4ml) e-oh (4)/2 = 10.25 (4)
[e-0.
e-0.6h-1
0.25-1
CAO [K2 (1-e-kit) - ki(1-e-k₂+),
= VB = XC CC = K₂cki
==
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