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 7E

(A)

Interpretation Introduction

Interpretation:

Estimate the fugacity of 1-propanol at temperature 300 K and pressure 1 bar using Peng-Robinson EOS.

Concept Introduction:

The expression of 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 of the reduced temperature (Tr) is,

Tr=TTc

Here, system temperature is T.

The expression of the compressibility factor (Z) is,

Z=PV_RT

(B)

Interpretation Introduction

Interpretation:

Estimate the fugacity of 1-propanol at temperature 300 K and pressure 5 bar using Peng-Robinson EOS.

(C)

Interpretation Introduction

Interpretation:

Estimate the fugacity of 1-propanol at temperature 400 K and pressure 3 bar using Peng-Robinson EOS.

(D)

Interpretation Introduction

Interpretation:

Estimate the fugacity of 1-propanol at temperature 500 K and pressure 10 bar using Peng-Robinson EOS.

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