Reamer, Sage and Lacey [Ind. Eng. Chem., 43, 1436 (1951)] measured the following compositions of phases in equilibrium for the methane/n-butane/n-decane system at 280°F and 3000 psia Species xi yi Metane 0.5444 0.9140 n-butane 0.0916 0.0512 n-decane 0.3640 0.0348 Use the Soave-Redlich-Kwong equation of state to predict the density, fugacity coefficients and the enthalpy of the mixture for each phase. Also, calculate the values of K and compare them with the experimental values obtained from the previous data.

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Reamer, Sage and Lacey [Ind. Eng. Chem., 43, 1436 (1951)] measured the
following compositions of phases in equilibrium for the methane/n-butane/n-decane
system at 280°F and 3000 psia
Species xi yi
Metane 0.5444 0.9140
n-butane 0.0916 0.0512
n-decane 0.3640 0.0348
Use the Soave-Redlich-Kwong equation of state to predict the density, fugacity
coefficients and the enthalpy of the mixture for each phase. Also, calculate the
values of K and compare them with the experimental values obtained from the
previous data.
Transcribed Image Text:Reamer, Sage and Lacey [Ind. Eng. Chem., 43, 1436 (1951)] measured the following compositions of phases in equilibrium for the methane/n-butane/n-decane system at 280°F and 3000 psia Species xi yi Metane 0.5444 0.9140 n-butane 0.0916 0.0512 n-decane 0.3640 0.0348 Use the Soave-Redlich-Kwong equation of state to predict the density, fugacity coefficients and the enthalpy of the mixture for each phase. Also, calculate the values of K and compare them with the experimental values obtained from the previous data.
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