I need help calculating enthalpies 1 through 4.
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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I need help calculating enthalpies 1 through 4.
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Example 8.4-4
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individual enthalpy changes for the three steps.
Partial Vaporization of a Mixture
An equimolar liquid mixture of benzene (B) and toluene (T) at 10°C is fed continuously to a vessel in which
the mixture is heated to 50°C. The liquid product is 40.0 mole% B, and the vapor product is 68.4 mole% B.
How much heat must be transferred to the mixture per g-mole of feed?
Basis: 1 mol Feed
1 mol, 10°C
0.500 mol B/mol
0.500 mol T/mol
We start with a degree-of-freedom analysis:
Q Search
CD
EVAPORATOR
H
ny(mol), 50°C
0.684 mol B/mol
0.316 mol T/mol
Q(J)
n₁ (mol), 50°C
0.400 mol B/mol
0.600 mol T/mol
3 unknown variables (ny, nL, Q)
-2 material balances
-1 energy balance
= 0 degrees of freedom
We could count each specific enthalpy to be determined as an unknown variable, but then we would also
count the equations for each of them in terms of heat capacities and latent heats, leaving the number of
degrees of freedom unchanged.
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Elementary Principles of Chemica X +
47°F
Partly sunny
File | E:/Elementary%20Principles%20of%20Chemical%20Processes,%204th%20Edition%20(%20PDF Drive%20).pdf
Draw
(T) Read aloud
Example 8.4-4
Solution
Equipment Encyclopedia
evaporator
www.wiley.com/college/felder
+
450 of 695
individual enthalpy changes for the three steps.
Partial Vaporization of a Mixture
An equimolar liquid mixture of benzene (B) and toluene (T) at 10°C is fed continuously to a vessel in which
the mixture is heated to 50°C. The liquid product is 40.0 mole% B, and the vapor product is 68.4 mole% B.
How much heat must be transferred to the mixture per g-mole of feed?
Basis: 1 mol Feed
1 mol, 10°C
0.500 mol B/mol
0.500 mol T/mol
We start with a degree-of-freedom analysis:
Q Search
CD
EVAPORATOR
H
ny(mol), 50°C
0.684 mol B/mol
0.316 mol T/mol
Q(J)
n₁ (mol), 50°C
0.400 mol B/mol
0.600 mol T/mol
3 unknown variables (ny, nL, Q)
-2 material balances
-1 energy balance
= 0 degrees of freedom
We could count each specific enthalpy to be determined as an unknown variable, but then we would also
count the equations for each of them in terms of heat capacities and latent heats, leaving the number of
degrees of freedom unchanged.
<
Ơ
re
80
J
^
ENG
Sign in
7:14 AM
5/6/2023
•
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+
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