Introduction to Chemical Engineering Thermodynamics
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: McGraw-Hill Education
Bartleby Related Questions Icon

Related questions

Question

Please help me answer at least all of the given questions. Thank you. 

PROBLEM 1:
A mixture of hydrocarbons with equal amounts of propane, i-butane, and n-butane exists at a pressure of 100 psia and
is all in the vapor phase.
a. What is the minimum temperature at which it could be a vapor?
b. What mole % of the vapor is condensed if the mixture is cooled to 90°F? What would be the liquid phase and vapor
phase compositions at this temperature?
c. What temperature is required to condense 100% of the vapor?
d.
If 100,000 ft at standard conditions of the original gas is introduced into a separator at 100 psia and 90°F, how many
metric tons of liquid have to be handled by the pump removing liquid from this separator?
e. What temperature is required to condense (at 100 psia) 40 mol % of the total vapor?
Component A
C3H8
i-C4H10
n-C4H10
Antoine equation:
log10 p*[bar] =A-
B
T[K]+C
B
C
4.53678 1149.36
24.906
4.3281 1132.108 0.918
4.35576 1175.581 -2.071
expand button
Transcribed Image Text:PROBLEM 1: A mixture of hydrocarbons with equal amounts of propane, i-butane, and n-butane exists at a pressure of 100 psia and is all in the vapor phase. a. What is the minimum temperature at which it could be a vapor? b. What mole % of the vapor is condensed if the mixture is cooled to 90°F? What would be the liquid phase and vapor phase compositions at this temperature? c. What temperature is required to condense 100% of the vapor? d. If 100,000 ft at standard conditions of the original gas is introduced into a separator at 100 psia and 90°F, how many metric tons of liquid have to be handled by the pump removing liquid from this separator? e. What temperature is required to condense (at 100 psia) 40 mol % of the total vapor? Component A C3H8 i-C4H10 n-C4H10 Antoine equation: log10 p*[bar] =A- B T[K]+C B C 4.53678 1149.36 24.906 4.3281 1132.108 0.918 4.35576 1175.581 -2.071
Expert Solution
Check Mark
Knowledge Booster
Background pattern image
Recommended textbooks for you
Text book image
Introduction to Chemical Engineering Thermodynami...
Chemical Engineering
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:McGraw-Hill Education
Text book image
Elementary Principles of Chemical Processes, Bind...
Chemical Engineering
ISBN:9781118431221
Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher:WILEY
Text book image
Elements of Chemical Reaction Engineering (5th Ed...
Chemical Engineering
ISBN:9780133887518
Author:H. Scott Fogler
Publisher:Prentice Hall
Text book image
Process Dynamics and Control, 4e
Chemical Engineering
ISBN:9781119285915
Author:Seborg
Publisher:WILEY
Text book image
Industrial Plastics: Theory and Applications
Chemical Engineering
ISBN:9781285061238
Author:Lokensgard, Erik
Publisher:Delmar Cengage Learning
Text book image
Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:9780072848236
Author:Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:McGraw-Hill Companies, The