Determinar el punto de Burbuja del siguiente sistema multicomponente
Constantes de Antoine 110
Benceno Tolueno Etil-benceno Presión (Kpa) 91.1925
A13.8594 14.0098 14.0045
B2773.78 3103.01 3279.47
C220.07 219.79 213.2
Compuesto P°
0.3 Benceno 234.10942748 2.35146098 0.7054382929
0.4 Tolueno 1.091747 99.559137846 1 0.4
0.3 Etil-benceno 47.352754921 0.4756244 0.1426873191
1.248125612
0.80120141 0.9159631348
73.0635596
T99.499962
Compuesto P°
0.3 Benceno 177.62473373 2.43109882 0.7293296472
0.4 Tolueno 0.80120141 73.063559566 1 0.4
0.3 Etil-benceno 33.680087447 0.4609697 0.1382909113
1.2676205585
0.7888796 1.248125612
71.939903
T98.9915811
Compuesto P°
0.3 Benceno 175.18510051 2.43515898 0.7305476929
0.4 Tolueno 0.7888796 71.939902987 1 0.4
0.3 Etil-benceno 33.109773672 0.46024212 0.1380726369
1.2686203298
0.7882579 1.2676205585
71.8832088
T98.965764
Compuesto P°
0.3 Benceno 175.06190048 2.43536569 0.7306097078
0.4 Tolueno 0.7882579 71.883208758 1 0.4
0.3 Etil-benceno 33.081021341 0.46020513 0.1380615386
1.2686712464
0.78822627 1.2686203298
71.8803238
T98.9644498
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𝑏𝑢𝑟𝑏𝑢𝑗𝑎
