f the mixture has an overall molar composition of 45% A and 55% B (binary mixture), find the following: A. Bubble temperature at 101.3 kPa, analytical solution assuming Raoult’s law B. Dew temperature at 101.3 kPa, analytical solution assuming Raoult’s law C. Create a Txy plot and find solutions for part A and B graphically assuming Raoult’s law
f the mixture has an overall molar composition of 45% A and 55% B (binary mixture), find the following: A. Bubble temperature at 101.3 kPa, analytical solution assuming Raoult’s law B. Dew temperature at 101.3 kPa, analytical solution assuming Raoult’s law C. Create a Txy plot and find solutions for part A and B graphically assuming Raoult’s law
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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If the mixture has an overall molar composition of 45% A and 55% B (binary mixture), find the following:
A. Bubble temperature at 101.3 kPa, analytical solution assuming Raoult’s law
B. Dew temperature at 101.3 kPa, analytical solution assuming Raoult’s law
C. Create a Txy plot and find solutions for part A and B graphically assuming Raoult’s law
![The image contains two equations related to the natural logarithm of the saturation pressure of components A and B, given in kilopascals (kPa):
1. \( \ln p_A^{\text{sat}} \, (\text{kPa}) = 16.1 - \frac{2900}{T(K) - 40} \)
2. \( \ln p_B^{\text{sat}} \, (\text{kPa}) = 15.9 - \frac{3000}{T(K) - 60} \)
These equations express the natural logarithm of the saturation pressures of two components A and B as functions of temperature in Kelvin (K). The constants and coefficients are specific to each component and are used to model the change in pressure with temperature.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F93114510-ea56-48dc-868a-4134db30fdae%2F374be1af-07fe-4c12-a817-bcce63da6fba%2F3tumq1c_processed.png&w=3840&q=75)
Transcribed Image Text:The image contains two equations related to the natural logarithm of the saturation pressure of components A and B, given in kilopascals (kPa):
1. \( \ln p_A^{\text{sat}} \, (\text{kPa}) = 16.1 - \frac{2900}{T(K) - 40} \)
2. \( \ln p_B^{\text{sat}} \, (\text{kPa}) = 15.9 - \frac{3000}{T(K) - 60} \)
These equations express the natural logarithm of the saturation pressures of two components A and B as functions of temperature in Kelvin (K). The constants and coefficients are specific to each component and are used to model the change in pressure with temperature.
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Step 1: Bubble and Dew Point temperatures at a constant pressure P
VIEWStep 2: Equations for Bubble Point and Dew point lines at constant P
VIEWStep 3: Vapour pressures by using ANTOINE equation
VIEWStep 4: T-X-Y data
VIEWStep 5: T-X-Y diagram
VIEWStep 6: Bubble and Dew points at X1=XA=0.45
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