Feed 5,500 kPa 30°C Retentate 5,450 kPa 30°C Membrane kmol/h separator kmol/h N2 CH4 200 N2 CH4 20 800 1,000 Permeate 100 kPa 30°C kmol/h N2 CH4 180
Feed 5,500 kPa 30°C Retentate 5,450 kPa 30°C Membrane kmol/h separator kmol/h N2 CH4 200 N2 CH4 20 800 1,000 Permeate 100 kPa 30°C kmol/h N2 CH4 180
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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Question
A new asymmetric, polyimide polymer membrane has been developed for the separation of N2 from CH4. At 30oC, permeance values are 50,000 and 10,000 barrer/cm for N2 and CH4, respectively.If this new membrane is used to perform the separation in Figure,determine the membrane surface area in m2, and the kmol/h of CH4 in the permeate. Base the driving force for diffusion on the arithmetic average of the partial pressures of the entering feed and the exiting retentate, with the permeate-side partial pressures at the exit condition.
![Feed
5,500 kPa
30°C
Retentate
5,450 kPa
30°C
Membrane
kmol/h
separator
kmol/h
N2
CH4
200
N2
CH4
20
800
1,000
Permeate
100 kPa
30°C
kmol/h
N2
CH4
180](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fa3ceee16-da77-4264-9713-63cf182d73e7%2F4614eb16-53cc-4fc2-95d5-dd1f8396ffea%2Fbjfs1uf.jpeg&w=3840&q=75)
Transcribed Image Text:Feed
5,500 kPa
30°C
Retentate
5,450 kPa
30°C
Membrane
kmol/h
separator
kmol/h
N2
CH4
200
N2
CH4
20
800
1,000
Permeate
100 kPa
30°C
kmol/h
N2
CH4
180
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