problema1,2y3flash

6
Zi A B C Pi* ki Benceno 0.4 6.01788 1203.677 219.904 179.995061 1.77685154 Tolueno 0.6 6.08436 1347.62 219.787 74.172425 0.73220558 100 °C F 100 kmol P° total 101.3 kpas V 72.1334791 kmol α 0.7213347907 fracción de vaporizac L 27.8665209 kmol f(α) 0 _^ ( )= ^ _ =( _ ^ )/

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ejemplo para calcular con excel el punto de roció , el punto de burbuja y la fracción vaporizada

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Problema1

ZiABCPi*kixiyiformula para encontrar :Benceno0.46.017881203.677219.904179.99506132951.77685154320.25634944810.4554949125Tolueno0.66.084361347.62219.78774.17242498590.73220557740.7436505570.5445050855

T100CF100kmoli=el numero de componentesP total101.3kpasV72.1334790653kmoli= Benceno, Tolueno.0.7213347907fraccin de vaporizacinL27.8665209347kmolf()-0

Problema2

ZiABCPi*kixiyiBenceno0.46.017881203.677219.904157.4693461.55448515540.28572052390.444148313Tolueno0.66.084361347.62219.78763.8537280.63034281950.81815941350.5157209115

P total101.3kpasT95.1383CTemperatura de Burbujaf(T)1.00000.7213347907

Problema3

ZiABCPi*kixiyiBenceno0.46.017881203.677219.90440.5200050.40000005240.70521965790.2820879001Tolueno0.66.084361347.62219.78713.9518620.13772815851.58724564840.2186084203

P total101.3kpasT53.0256CTemperatura de Rociof(T)1.00000.7213347907