13013043_VLE
5
NAMA : Hendi Aviano Prasetyo NIM : 13013043 Kesetimbangan uap-cair sistem 1-butanol (1)/etanol(2) Informasi titik didih komponen pada 1 atm 1-butanol = 117.6 °C etanol = 78.4 °C Data kesetimbangan uap - cair sistem 1-butanol(1)/etanol(2) pada tekanan 0,95 bar TEMPERATUR (°C) x 1 (mol/mol) y 1 (mol/mol) 76.6724 0 0 77.0691 0.01 0.0021163 77.2724 0.02 0.0042659 77.4773 0.03 0.0064499 77.6837 0.04 0.0086693 78.1015 0.06 0.0132188 78.5261 0.08 0.0179235 78.958 0.1 0.0227932 80.0712 0.15 0.0357589 81.2371 0.2 0.0500034 82.462 0.25 0.0657408 83.7527 0.3 0.0832264 85.1168 0.35 0.102768 86.563 0.4 0.12474 88.1012 0.45 0.149601 89.7427 0.5 0.177923 91.5006 0.55 0.21042 93.3906 0.6 0.248 95.4309 0.65 0.291831 97.6434 0.7 0.343432 100.055 0.75 0.404814 102.696 0.8 0.478679 105.608 0.85 0.56873 108.836 0.9 0.680133 110.229 0.92 0.73223 111.685 0.94 0.789492 113.209 0.96 0.852628 113.998 0.97 0.886653 114.806 0.98 0.922469 115.633 0.99 0.960205 116.032 1 1
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Transcript of 13013043_VLE
NAMA : Hendi Aviano Prasetyo
NIM : 13013043
Kesetimbangan uap-cair sistem 1-butanol (1)/etanol(2)
Informasi titik didih komponen pada 1 atm
1-butanol = 117.6 °C
etanol = 78.4 °C
Data kesetimbangan uap - cair sistem 1-butanol(1)/etanol(2) pada tekanan 0,95 bar
TEMPERATUR
(°C)x1 (mol/mol)
y1
(mol/mol)
76.6724 0 0
77.0691 0.01 0.0021163
77.2724 0.02 0.0042659
77.4773 0.03 0.0064499
77.6837 0.04 0.0086693
78.1015 0.06 0.0132188
78.5261 0.08 0.0179235
78.958 0.1 0.0227932
80.0712 0.15 0.0357589
81.2371 0.2 0.0500034
82.462 0.25 0.0657408
83.7527 0.3 0.0832264
85.1168 0.35 0.102768
86.563 0.4 0.12474
88.1012 0.45 0.149601
89.7427 0.5 0.177923
91.5006 0.55 0.21042
93.3906 0.6 0.248
95.4309 0.65 0.291831
97.6434 0.7 0.343432
100.055 0.75 0.404814
102.696 0.8 0.478679
105.608 0.85 0.56873
108.836 0.9 0.680133
110.229 0.92 0.73223
111.685 0.94 0.789492
113.209 0.96 0.852628
113.998 0.97 0.886653
114.806 0.98 0.922469
115.633 0.99 0.960205
116.032 1 1
Data kesetimbangan uap-cairsistem 1-butanol(1)/etanol(2) pada T=95°C
Tekanan Uap
(kPa)x1 (mol/mol)
y1
(mol/mol)
189.615 0 0
188.162 0.01 0.0023483
186.71 0.02 0.0047276
185.259 0.03 0.0071388
183.809 0.04 0.0095828
180.912 0.06 0.0145731
178.017 0.08 0.0197064
175.125 0.1 0.0249912
167.9 0.15 0.0389259
160.679 0.2 0.0540214
153.454 0.25 0.0704625
146.22 0.3 0.0884702
138.973 0.35 0.108311
131.709 0.4 0.130313
124.425 0.45 0.154877
117.117 0.5 0.182512
109.785 0.55 0.213862
102.425 0.6 0.249762
95.0374 0.65 0.291312
87.6203 0.7 0.339994
80.1732 0.75 0.397852
72.6955 0.8 0.467787
65.1866 0.85 0.554066
57.6465 0.9 0.663222
54.6217 0.92 0.715453
51.5918 0.94 0.773894
48.557 0.96 0.839727
47.0377 0.97 0.875868
45.5171 0.98 0.91445
43.9953 0.99 0.955729
42.4723 1 1
70
80
90
100
110
120
130
0 0.2 0.4 0.6 0.8 1 1.2
T (oC)
x1,y1 (mol/mol)
Grafik P-x-y Kesetimbangan Uap Cairsistem 1-butanol(1)/etanol(2) pada T= 95
°C (isotermal)
P-x1
P-y1
0
0.2
0.4
0.6
0.8
1
1.2
0 0.2 0.4 0.6 0.8 1 1.2
y1 (mol/mol)
x1 (mol/mol)
Grafik x-y Kesetimbangan Uap Cairsistem 1-butanol(1)/etanol(2)
pada P = 0,95 bar (isobar)
0
50
100
150
200
250
0 0.2 0.4 0.6 0.8 1 1.2
P (kPa)
x1,y1 (mol/mol)
Grafik T-x-y Kesetimbangan Uap Cairsistem 1-butanol(1)/etanol(2) pada
P=0,95 bar (isobar)
T-x1
T-y1
0
0.2
0.4
0.6
0.8
1
1.2
0 0.2 0.4 0.6 0.8 1 1.2
y1 (mol/mol)
x1 (mol/mol)
Grafik x-y Kesetimbangan Uap Cairsistem 1-butanol(1)/etanol(2)
pada T= 95°C (isotermal)
sumber data/daftar pustaka
Anonim. http://vle-calc.com/phase_diagram.html?numOfC=2&
compnames=1&Comp1=12&Comp2=5&Comp3=2&VLEMode=isobaric&VLEType=xy
&numberForVLE=0.95 diakses pada 28 September 2015
DDBST - Dortmund Data Bank Software and Separation Technology GmbH
J. Gmehling and co.: Vapor-Liquid Equilibrium Data Collection series, 1981 Dechema
KDB Binary VLE Database diakses pada tanggal 8 September 2015
R. H. Perry, Don W. Green: Perry's Chemical Engineers' Handbook, 1999 McGraw-Hill Inc.
