Download presentation

Presentation is loading. Please wait.

Published byRobin Willmott Modified over 2 years ago

1
**Fugacity of Non-Ideal Mixtures (SVNA 11.6 and 11.7)**

In our attempt to describe the Gibbs energy of real gas and liquid mixtures, we examine two “sources” of non-ideal behaviour: Pure component non-ideality due to PVT behaviour concept of fugacity Non-ideality in mixtures partial molar properties mixture fugacity and residual properties We will begin our treatment of non-ideality in mixtures by considering gas behaviour. Start with an ideal gas mixture expression. Modify this expression for cases where pure component non-ideality is observed. Further modify this expression for cases in which non-ideal mixing effects occur. CHEE 311 Lecture 11

2
**Ideal Gas Mixtures In an ideal gas mixture**

all molecules have negligible volume interactions between molecules of any type are negligible. Based on this model, the chemical potential of any component in a perfect gas mixture is: where the reference state, Giig(T,P) is the pure component Gibbs energy at the given P,T. For a pure ideal gas, we derived: CHEE 311 Lecture 11

3
**Ideal Gas Mixtures Substitute to get: (11.29)**

which is the chemical potential of component i in an ideal gas mixture at T,P. The total Gibbs energy of the ideal gas mixture is the sum of the contributions from the individual components: (11.11) (11.30) CHEE 311 Lecture 11

4
**Ideal Mixtures of Real Gases**

Consider an ideal solution of real gases. The molecules have finite volume and interact, but assume these interactions are equivalent between components The appropriate model is that of an ideal solution: where Gi(T,P) is the Gibbs energy of the real pure gas: (11.31) Our ideal solution model applied to real gases is therefore: CHEE 311 Lecture 11

5
**Non-Ideal Mixtures of Real Gases**

In cases where molecular interactions differ between the components (polar/non-polar mixtures) the ideal solution model does not apply Our knowledge of pure component fugacity is of little use in predicting the mixture properties We require experimental data or correlations pertaining to the specific mixture of interest To cope with highly non-ideal gas mixtures, we define a mixture fugacity: (11.47) where fi is the fugacity of species i in solution, which replaces the product yiP in the perfect gas model, and yifi of the ideal solution model. CHEE 311 Lecture 11

6
**Non-Ideal Mixtures of Real Gases**

To describe non-ideal gas mixtures, we define the solution fugacity: and the fugacity coefficient for species i in solution: (11.52) In terms of the solution fugacity coefficient: Notation: fi, i - fugacity and fugacity coefficient for pure species i fi, i - fugacity and fugacity coefficient for species i in solution CHEE 311 Lecture 11

7
**Calculating iv from Compressibility Data**

Consider a two-component vapour of known composition at a given pressure and temperature If we wish to know the chemical potential of each component, we must calculate their respective fugacity coefficients In the laboratory, we could prepare mixtures of various composition and perform PVT experiments on each. For each mixture, the compressibility (Z) of the gas can be measured from zero pressure to the given pressure. For each mixture, an overall fugacity coefficient can be derived at the given P,T: How do we use this overall fugacity coefficient to derive the fugacity coefficients of each component in the mixture? CHEE 311 Lecture 11

8
**Calculating iv from Compressibility Data**

The mixture fugacity coefficients are partial molar properties of the residual Gibbs energy, and hence partial molar properties of the overall fugacity coefficient: In terms of our measured compressibility: CHEE 311 Lecture 11

9
**Calculating iv from the Virial EOS**

We know how to use the virial equation of state to calculate the fugacity and fugacity coefficient of pure, non-polar gases at moderate pressures. The virial equation can be generalized to describe the calculation of mixture properties. The truncated virial equation is the simplest alternative: where B is a function of temperature and composition according to: (11.61) Bij characterizes binary interactions between i and j; Bij=Bji CHEE 311 Lecture 11

10
**Calculating iv from the Virial EOS**

Pure component coefficients (B11≡ B1, B22≡ B2,etc) are calculated as previously and cross coefficients are found from: (11.69b) where, and ( ] Bo and B1 for the binary pairs are calculated using the standard equations 3.65 and 3.66 using Tr=T/Tcij. CHEE 311 Lecture 11

11
**Calculating iv from the Virial EOS**

We now have an equation of state that represents non-ideal PVT behaviour of mixtures: or We are equipped to calculate mixture fugacity coefficients from equation 11.60 CHEE 311 Lecture 11

12
**Calculating iv from the Virial EOS**

The result of differentiation is: (11.64) with the auxiliary functions defined as: In the binary case, we have (11.63a) (11.63b) CHEE 311 Lecture 11

13
**6. Calculating iv from the Virial EOS**

Method for calculating mixture fugacity coefficients: 1. For each component in the mixture, look up: Tc, Pc, Vc, Zc, 2. For each component, calculate the virial coefficient, B 3. For each pair of components, calculate: Tcij, Pcij, Vcij, Zcij, ij and using Tcij, Pcij for Bo,B1 4. Calculate ik, ij and the fugacity coefficients from: CHEE 311 Lecture 11

Similar presentations

Presentation is loading. Please wait....

OK

CHEMICAL AND PHASE EQUILIBRIUM (1)

CHEMICAL AND PHASE EQUILIBRIUM (1)

© 2018 SlidePlayer.com Inc.

All rights reserved.

Ads by Google

Ppt on remote operated spy robot remote Ppt on measures of central tendency Ppt on beer lambert law example Ppt on shell scripting youtube Ppt on historical and heritage site tourism Download ppt on subject and predicate Ppt on resistance temperature detector formula Accounting standard 20 earning per share ppt online Ppt on abstract class in java Ppt on earth dam stability