1. Calculate the fugacity of CO at 50 bar and 400 bar, if the following data are applicable at 273 K. P, bar 25 50 100 0.9890 0.9792 0.9741

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
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7:36 M
I♥Z 27% O
**
<***
1. Calculate the fugacity of CO at 50 bar and
400 bar, if the following data are applicable
at 273 K.
P, bar
25
50
100
0.9890
0.9792
0.9741
2. Calculate the fugacity of methane as at 322
K and 55 bar, given that the critical
constants are 190.7 K and 46.4 bar.
3. Calculate the fugacity of nitrogen at 800
bar from the following data at 273 K.
P, bar
PV/RT
50
100
200
0.9846
0.9846
1.0365
4. Estimate the fugacity of gaseous propane
at 12 bar and 310 K using the following
data
P, bar
V, m/kg
1.7
3.4
6.8
0.3313
0.1609
0.0754
Also, compute the fugacity of propane at 310 K
and 70 bar given that the vapour pressure of
propane at 310 K is 13 bar.
Transcribed Image Text:7:36 M I♥Z 27% O ** <*** 1. Calculate the fugacity of CO at 50 bar and 400 bar, if the following data are applicable at 273 K. P, bar 25 50 100 0.9890 0.9792 0.9741 2. Calculate the fugacity of methane as at 322 K and 55 bar, given that the critical constants are 190.7 K and 46.4 bar. 3. Calculate the fugacity of nitrogen at 800 bar from the following data at 273 K. P, bar PV/RT 50 100 200 0.9846 0.9846 1.0365 4. Estimate the fugacity of gaseous propane at 12 bar and 310 K using the following data P, bar V, m/kg 1.7 3.4 6.8 0.3313 0.1609 0.0754 Also, compute the fugacity of propane at 310 K and 70 bar given that the vapour pressure of propane at 310 K is 13 bar.
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