4. A diffusion-convection system is shown to the right, in which liquid A is evaporating into gas B. The liquid level is kept constant at z = z1. At the liquid-gas interface, the gas phase mole fraction of A is XA1. A stream of gas mixture A-B of concentration XA2 flows slowly past the top of the tube, to maintain the mole fraction of A at XA2 at Z = Z2. The entire system is kept at constant temperature and pressure. Gases A and B are assumed to be ideal. This evaporating system is at steady state, and there is a net motion of A away from the interface and the species B is stationary. The rate of evaporation of A is as follows: NAz = CD AB InB2 Z2-Z1 XB1 Derive the above expression, starting with the following equation: Gas stream of A and B z=22 + Az NA + ↑ NA:\ z=2₁ Liquid A дха NAZ = XA(NAZ +1 +NBz)-CDAB dz Note that XA is not small and cannot be omitted. Derive the rate of evaporation of A without finding the concentration profile. Use a shell balance to determine in Naz is constant.
4. A diffusion-convection system is shown to the right, in which liquid A is evaporating into gas B. The liquid level is kept constant at z = z1. At the liquid-gas interface, the gas phase mole fraction of A is XA1. A stream of gas mixture A-B of concentration XA2 flows slowly past the top of the tube, to maintain the mole fraction of A at XA2 at Z = Z2. The entire system is kept at constant temperature and pressure. Gases A and B are assumed to be ideal. This evaporating system is at steady state, and there is a net motion of A away from the interface and the species B is stationary. The rate of evaporation of A is as follows: NAz = CD AB InB2 Z2-Z1 XB1 Derive the above expression, starting with the following equation: Gas stream of A and B z=22 + Az NA + ↑ NA:\ z=2₁ Liquid A дха NAZ = XA(NAZ +1 +NBz)-CDAB dz Note that XA is not small and cannot be omitted. Derive the rate of evaporation of A without finding the concentration profile. Use a shell balance to determine in Naz is constant.
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
![4.
A diffusion-convection system is shown to the right, in
which liquid A is evaporating into gas B. The liquid level is kept
constant at z = z1. At the liquid-gas interface, the gas phase mole
fraction of A is XA1. A stream of gas mixture A-B of concentration
XA2 flows slowly past the top of the tube, to maintain the mole
fraction of A at XA2 at Z = Z2. The entire system is kept at constant
temperature and pressure. Gases A and B are assumed to be ideal.
This evaporating system is at steady state, and there is a net motion
of A away from the interface and the species B is stationary. The rate
of evaporation of A is as follows:
NAz
=
CD
AB InB2
Z2-Z1 XB1
Derive the above expression, starting with the following equation:
Gas stream of A and B
z=22
+
Az
NA +
↑
NA:\
z=2₁
Liquid A
дха
NAZ = XA(NAZ +1
+NBz)-CDAB
dz
Note that XA is not small and cannot be omitted. Derive the rate of evaporation of A without
finding the concentration profile. Use a shell balance to determine in Naz is constant.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F76a241b1-3148-428a-9d7b-4a1276447a9a%2F022e47e0-9385-459b-9800-2b332ad487f6%2Ftudaqul_processed.jpeg&w=3840&q=75)
Transcribed Image Text:4.
A diffusion-convection system is shown to the right, in
which liquid A is evaporating into gas B. The liquid level is kept
constant at z = z1. At the liquid-gas interface, the gas phase mole
fraction of A is XA1. A stream of gas mixture A-B of concentration
XA2 flows slowly past the top of the tube, to maintain the mole
fraction of A at XA2 at Z = Z2. The entire system is kept at constant
temperature and pressure. Gases A and B are assumed to be ideal.
This evaporating system is at steady state, and there is a net motion
of A away from the interface and the species B is stationary. The rate
of evaporation of A is as follows:
NAz
=
CD
AB InB2
Z2-Z1 XB1
Derive the above expression, starting with the following equation:
Gas stream of A and B
z=22
+
Az
NA +
↑
NA:\
z=2₁
Liquid A
дха
NAZ = XA(NAZ +1
+NBz)-CDAB
dz
Note that XA is not small and cannot be omitted. Derive the rate of evaporation of A without
finding the concentration profile. Use a shell balance to determine in Naz is constant.
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