Fundamentals of Chemical Engineering Thermodynamics (MindTap Course List)
Fundamentals of Chemical Engineering Thermodynamics (MindTap Course List)
1st Edition
ISBN: 9781111580704
Author: Kevin D. Dahm, Donald P. Visco
Publisher: Cengage Learning
Question
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Chapter 8.6, Problem 21P

(A)

Interpretation Introduction

Interpretation:

The vapor pressure at T=25°C.

Concept Introduction:

The Peng-Robinson equation is,

P=RTV_baV_(V_+b)+b(V_b)

Here, molar volume is V_, parameters of Robinson equation are a, b, gas constant is R, temperature and pressure is T and P respectively.

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

κ=0.37464+1.54226ω0.26993ω2

The expression to obtain the relative temperature at the critical point 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 of compressibility factor is,

Z=PV_RT

The residual properties of A is,

A=aPR2T2

The residual properties of B is,

B=bPRT

The expression of fugacity of a compound as described by the Peng-Robinson equation is,

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

(B)

Interpretation Introduction

Interpretation:

The fugacity at the critical point.

(C)

Interpretation Introduction

Interpretation:

The fugacity of saturated liquid at T=25°C.

(D)

Interpretation Introduction

Interpretation:

The fugacity of compressed liquid at T=25°C and P=500 bar.

Concept Introduction:

The Poynting equation to obtain fugacity in liquid phase at 500 bar is,

fL=fsatexp[V_(P2Psat)RT]

Here, saturated pressure is Psat, molar volume is V_, and saturated vapor fugacity is fsat.

(E)

Interpretation Introduction

Interpretation:

The normal boiling point.

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