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Name: |
Threeq1 - Dew point of a nonideal binary mixture
(isobutanol-water) |
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Source: |
Henley, E. J. and Rosen, E. M., Material
and Energy Balance |
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Computations, Wiley:
New York, 1969 |
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Reference/s |
Shacham, M., N. Brauner and M. Pozin, Computers
chem. Engng., 22,321-323(1998) |
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Model: |
3 implicit equations, indep. variables t,
x1 and x2 |
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Average difficulty level |
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Constraints: 0<=x1<=1, 0<=x2<=1 |
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Discontinuities: Undefined for t=-191.15 or
t=-235 |
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Initial estimates: 1. t=100, x1=0.2, x2=0.8,
2. t=70, x1=0.5, x2=0.5; |
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3. t=80, x1=0.2, x2=0.8 4. t=80, x1=0.5, x2=0.5 |
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Solved by |
Shacham, M., POLYMATH 5.1, build 19, April
3, 2001 |
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Model Eqs. |
Dew point of a nonideal binary mixture (isobutanol-water)
|POLVER05_1 |
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EXCEL
FILE |
f(t)=x1+x2-1 # |
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TEXT
FILE |
f(x1)=x1-y1/k1 # |
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POLYMATH
FILE |
f(x2)=x2-y2/k2 # |
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y2=0.8 # |
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y1=0.2 # |
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p1=10^(7.62231-1417.9/(191.15+t)) # |
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p2=10^(8.10765-1750.29/(235+t)) # |
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B=0.7 # |
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A=1.7 # |
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gamma2=10^(B*x1*x1/((x1+B*x2/A)^2)) # |
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gamma1=10^(A*x2*x2/((A*x1/B+x2)^2)) # |
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k2=gamma2*p2/760 # |
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k1=gamma1*p1/760 # |
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t(0)=100 |
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x1(0)=0.2 |
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x2(0)=0.8 |
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Variable/function values |
Variable |
Value |
f(x) |
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t |
100 |
0.0000E+00 |
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x1 |
0.2 |
1.4093E-01 |
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x2 |
0.8 |
1.6744E-01 |
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y2 |
0.8 |
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y1 |
0.2 |
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p1 |
565.34 |
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p2 |
763.67 |
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B |
0.7 |
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A |
1.7 |
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gamma2 |
1.26 |
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gamma1 |
4.55 |
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k2 |
1.26 |
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k1 |
3.39 |
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Solution |
Variable |
Value |
f(x) |
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t |
93.96706523770 |
0.0000E+00 |
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x1 |
0.0078754574659 |
2.6021E-17 |
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x2 |
0.9921245425339 |
-6.66E-16 |
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y2 |
0.8 |
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y1 |
0.2 |
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p1 |
445.92824865560 |
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p2 |
612.47305384950 |
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B |
0.7 |
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A |
1.7 |
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gamma2 |
1.0005767327950 |
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gamma1 |
43.28155074142 |
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k2 |
0.8063503778230 |
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k1 |
25.39535015950 |
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Additional Information |
Some of the methods do not converge from initial
guesses 3 and 4 |