For the overall composition below, please use the DePriester Charts to determine (a) the temperature and (b) the composition of the liquid phase at the dew point when the system is at 100 psia. ZCH, = 0.5 = 0.43 = 0.07

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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De Priester chart values are also attached with the question
DePriester Chart Values
2 December 2019
60 psia
530PR
Pressure
Enter the pressure in psia in Cell F6
Temperature
Enter the temperature in °R in Cell F7
Species Species #
K
In(K)
a72
a16
api
In(P)
ap2
ap3
a/T2
a16
appln(P)
apz/p2
apa/P
Methane
1
34.942323 3.5536988 -292860
8.2445
-0.8951 4.0943446 59.8465
-1.042577
8.2445
-3.6648478 0.016624
Ethylene
2
10.121341 2.3146462 -600077
7.90595
-0.84677 4.0943446 42.94594
-2.136265
7.90595
-3.4669681 0.0119294
Ethane
3
6.3368083 1.8463752 -687248
7.90694
-0.886
4.0943446 49.02654
-2.446594
7.90694 -3.6275893 0.0136185
7.71725
Propylene
Propane
4
1.9681902 0.6771144 -970689
-0.87871 4.0943446 47.67624
-3.455637
7.71725 -3.5977415 0.0132434
1.930926 0.6579997 -970689
7.15059
-0.76984 4.0943446
6.90224
-3.455637
7.15059
-3.1519902
0.1150373
Iso-Butane
6
0.8164472 -0.202793 -1166846
7.72668
-0.92213 4.0943446
-4.153955
7.72668
-3.775518
n-Butane
7
0.5722927 -0.558105 -1280557
7.94986
-0.96455 4.0943446
-4.558765
7.94986
-3.9492
Iso-Pentane
8.
0.2213622 -1.507955 -1481583
7.58071
-0.93159 4.0943446
-5.274414
7.58071 -3.8142505
n-Pentane
9.
0.1742748 -1.747122 -1524891
7.33129
-0.89143 4.0943446
-5.42859
7.33129 -3.6498216
n-Hexane
10
0.0589987 -2.83024 -1778901
6.96783
-0.84634 4.0943446
-6.332862
6.96783 -3.4652076
11
0.0203081 -3.896734 -2013803
6.52914
-0.79543 4.0943446
-7.16911
6.52914 -3.2567645
n-Heptane
n-Octane
12
0.0071655 -4.93848
-7646.816 12.48457
-0.73152 4.0943446
-14.42796 12.48457 -2.9950949
n-Nonane
13
0.0021012 -6.165239 -2551040
5.69313
-0.67818 4.0943446
-9.081666
5.69313 -2.7767026
n-Decane
14
0.0005321 -7.538645
-9760.457 13.80354
-0.7147 4.0943446
-18.41596 13.80354 -2.9262281
Transcribed Image Text:DePriester Chart Values 2 December 2019 60 psia 530PR Pressure Enter the pressure in psia in Cell F6 Temperature Enter the temperature in °R in Cell F7 Species Species # K In(K) a72 a16 api In(P) ap2 ap3 a/T2 a16 appln(P) apz/p2 apa/P Methane 1 34.942323 3.5536988 -292860 8.2445 -0.8951 4.0943446 59.8465 -1.042577 8.2445 -3.6648478 0.016624 Ethylene 2 10.121341 2.3146462 -600077 7.90595 -0.84677 4.0943446 42.94594 -2.136265 7.90595 -3.4669681 0.0119294 Ethane 3 6.3368083 1.8463752 -687248 7.90694 -0.886 4.0943446 49.02654 -2.446594 7.90694 -3.6275893 0.0136185 7.71725 Propylene Propane 4 1.9681902 0.6771144 -970689 -0.87871 4.0943446 47.67624 -3.455637 7.71725 -3.5977415 0.0132434 1.930926 0.6579997 -970689 7.15059 -0.76984 4.0943446 6.90224 -3.455637 7.15059 -3.1519902 0.1150373 Iso-Butane 6 0.8164472 -0.202793 -1166846 7.72668 -0.92213 4.0943446 -4.153955 7.72668 -3.775518 n-Butane 7 0.5722927 -0.558105 -1280557 7.94986 -0.96455 4.0943446 -4.558765 7.94986 -3.9492 Iso-Pentane 8. 0.2213622 -1.507955 -1481583 7.58071 -0.93159 4.0943446 -5.274414 7.58071 -3.8142505 n-Pentane 9. 0.1742748 -1.747122 -1524891 7.33129 -0.89143 4.0943446 -5.42859 7.33129 -3.6498216 n-Hexane 10 0.0589987 -2.83024 -1778901 6.96783 -0.84634 4.0943446 -6.332862 6.96783 -3.4652076 11 0.0203081 -3.896734 -2013803 6.52914 -0.79543 4.0943446 -7.16911 6.52914 -3.2567645 n-Heptane n-Octane 12 0.0071655 -4.93848 -7646.816 12.48457 -0.73152 4.0943446 -14.42796 12.48457 -2.9950949 n-Nonane 13 0.0021012 -6.165239 -2551040 5.69313 -0.67818 4.0943446 -9.081666 5.69313 -2.7767026 n-Decane 14 0.0005321 -7.538645 -9760.457 13.80354 -0.7147 4.0943446 -18.41596 13.80354 -2.9262281
For the overall composition below, please use the DePriester Charts to determine (a) the temperature
and (b) the composition of the liquid phase at the dew point when the system is at 100 psia.
3.
ZCH,
= 0.5
ZC,H = 0.43
= 0.07
Transcribed Image Text:For the overall composition below, please use the DePriester Charts to determine (a) the temperature and (b) the composition of the liquid phase at the dew point when the system is at 100 psia. 3. ZCH, = 0.5 ZC,H = 0.43 = 0.07
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