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
Related questions
Question
100%
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

Transcribed Image Text:V =
TA =
0.00596(1 − XA)0.94671
FAO = CAOVO
→V=
FAOXA
(-ra)_exit
VCSTR =
YAO (P
УАО
CAO = (G)
Rgas (T)
FAO = CAOVO = 0.1443
FAOXA
0.5 10atm
L. atm
mol.k
mol
L
-ra) Exit
CAoVOXA
0.00596(1XA) 0.9467
0.08206
= 0.144
(422.2k)
mol
L
*6=0.8659
S
S
(0.865908 mol) (XA)
S
0.00596(1X)0.94671.
mol
L
mol
L*S

Transcribed Image Text:Feed stream
CAO? gmole * L-1
YAO = 0.5
Vo = 6L*s-1
Knowns:
H
V =
CAO =
V = ? L
XA =
ΧΑ
УАО
Rgas T
A =
FAOXA
(-A)_exit
=
=
T = 422.2 K
P
Product stream
0.00596(1X) 0.94671
FA0 =
V =
= 10 atm
0.08206
FAO CAOVO = 0.1443
CAovo
0.5 10atm
L. atm
mol.k
mol L
L
Cao VoXA
0.00596(1XA) 0.940
(422.2k)
= 0.144.
*6 = 0.8659
S
mol
L
mol
S
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