High-Pressure Vapor-Liquid Equilibrium Data for a Binary Mixture: the Poynting Factor Correction

​
pressure in kPa
303.975
option
isobaric VLE diagram
Consider a binary mixture composed of
n
-hexane and
n
-heptane. This Demonstration computes and plots the isobaric vapor-liquid equilibrium diagram, the equilibrium curve, the relative volatility, the
K
-value, the gas-phase fugacity coefficients using the Soave–Redlich–Kwong equation of state (EOS), and the Poynting correction factor for user-specified values of the pressure. The Demonstration takes into account deviation from ideal behavior in the gas phase by including gas phase fugacity coefficients. Thus high-pressure VLE data can be obtained. This Demonstration allows for the Poynting factor correction. Snapshots present calculations at a pressure approximately equal to 303.975 kPa.
VLE data is computed using the following formula (the gamma-phi-poy equation):
ϕ
i
y
i
P=
g
i
x
i
sat
P
i
exp
L
v
i
P-
sat
P
i

RT
, where
y
i
and
x
i
are the vapor and liquid mole fractions of component
i
,
P
is the total pressure,
sat
P
i
is the saturation vapor pressure of component
i
,
ϕ
i
is the vapor-phase fugacity coefficient, and
g
i
is the liquid-phase activity coefficient, where
ϕ
i
and
g
i
are determined using the Soave–Redlich–Kwong equation of state and the Wilson model, respectively;
L
v
i
is the liquid molar volume of molecule
i
determined using the Rackett equation.

Details

For more information about pressure effects, the Rackett equation, and the Pitzer–Curl method, see
[1] M. F. Doherty and M. F. Malone, Conceptual Design of Distillation Systems, New York: McGraw-Hill, 2001.
[2] B. E. Poling, J. M. Prausnitz, and J. P. O'Connell, The Properties of Gases and Liquids, 5th ed., New York: McGraw-Hill, 2004.
For more information about the SRK equation of state and the Wilson activity coefficients, see
[3] S. I. Sandler, Chemical and Engineering Thermodynamics, New York: John Wiley & Sons, 1999.
[4] J. R. Elliot and C. T. Lira, Introductory Chemical Engineering Thermodynamics, Upper Saddle River, NJ: Prentice Hall, 1999.

Permanent Citation

Housam Binous
​
​"High-Pressure Vapor-Liquid Equilibrium Data for a Binary Mixture: the Poynting Factor Correction"​
​http://demonstrations.wolfram.com/HighPressureVaporLiquidEquilibriumDataForABinaryMixtureThePo/​
​Wolfram Demonstrations Project​
​Published: March 7, 2011