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 8.5, Problem 6E

(A)

Interpretation Introduction

Interpretation:

The fugacity of butane at temperature 300 K and pressure 0.5 bar.

Concept Introduction:

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 Peng-Robinson equation is,

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

Here, pressure is P, 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 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

Here, gas constant is R.

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 (Z) for liquid phase is,

ZL=PV_LRT

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

A=aPR2T2

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

B=bPRT

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

ln(fLP)=(ZL1)ln(ZLB)A2B2ln[ZL+(1+2)BZL+(12)B]

The expression of compressibility factor (Z) is,

ZV=PV_VRT

(B)

Interpretation Introduction

Interpretation:

The fugacity of butane at temperature 350 K and pressure 5 bar.

(C)

Interpretation Introduction

Interpretation:

The fugacity of butane at temperature 400 K and pressure 1 bar.

(D)

Interpretation Introduction

Interpretation:

The fugacity of butane at temperature 500 K and pressure 10 bar.

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