Fundamentals Of Chemical Engineering Thermodynamics
Fundamentals Of Chemical Engineering Thermodynamics
1st Edition
ISBN: 9781111580711
Author: Kevin D. Dahm, Donald P. Visco, Jr.
Publisher: CENGAGE L
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Chapter 8.5, Problem 8E
Interpretation Introduction

Interpretation:

The fugacity of the compound in the liquid phase at temperature 300 K and various pressures 1, 10, 100 and 1000 bar.

Concept Introduction:

The Poynting equation to estimate the fugacity (f) of the compound in the solid phase is,

f=fsatexp{V_(PPsat)RT}

Here, molar volume is V_, pressure is P, vapor pressure is Psat, gas constant is R, temperature is T, and the fugacity of a liquid or vapor that is at its vapor pressure is fsat.

The expression to obtain the parameter used in calculation of a for Peng-Robinson EOS is,

κ=0.37464+1.54226ω0.26993ω2

Here, parameter is κ.

The expression to obtain the reduced temperature (Tr) is,

Tr=TTc

Here, system temperature is T.

The expression to obtain the value of α expressed as a function of the reduced temperature is,

α=[1+κ(1Tr0.5)]2

The expression to obtain the value of parameter a at the critical point is,

ac=0.45724R2Tc2Pc

The expression to obtain the parameter a is,

a=acα

The expression to obtain the parameter b is,

b=0.07780RTcPc

The expression to obtain the compressibility factor (Z) is,

Z=PV_RT

The expression to obtain the dimensionless group that include the Peng-Robinson parameter (A) is,

A=aPR2T2

The expression to obtain the dimensionless group that include the Peng-Robinson parameter (B) is,

B=bPRT

The fugacity (fsat) of a compound as described by the Peng-Robinson equation is,

ln(fsatP)=(Z1)ln(ZB)A2B2ln[Z+(1+2)BZ+(12)B]

The vapor pressure using Antoine equation is,

Psat=10[ABC+T(°C)]

Here, temperature in degree Celsius is T(°C), and Antoine coefficients are A,B,andC.

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