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Chemical Engineering Department | University of Jordan | Amman 11942, Jordan Tel. +962 6 535 5000 | 22888 1 Dr.-Eng. Zayed Al-Hamamre Thermodynamics II G E models and VLE data Chemical Engineering Department | University of Jordan | Amman 11942, Jordan Tel. +962 6 535 5000 | 22888 2 Review

Lec 7-GE models and VLE data.ppt

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Page 1: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

1

Dr.-Eng. Zayed Al-Hamamre

Thermodynamics II

GE models and VLE data

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

2

Review

Page 2: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

3

Review

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

4

Determination of GE from Experimental Data

Page 3: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

5

Determination of GE from Experimental Data

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

6

Example

Page 4: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

7

Example cont.

Starting with modified Raoult's law;

Values are known at state 1

Calculate

The same for component two, get

Use At state 1 to get

= 0.4

= 0.7= 1 bar

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

8

Example

Use the values ofCalculate new

Then, at state 2 for component 1 = 0.8 = 1 bar

for component 1 2 2 2 2

Knowing that

Solve for P

Page 5: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

9

Example cont.

For binary mixture

Then get

at known x1, x2 and

Show this

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

10

Example cont.

Then

At the given conditions:

Page 6: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

11

Example cont.

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

12

Example cont.

Page 7: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

13

Example cont.

Unknowns,

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

14

Example cont.

Page 8: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

15

What does this mean?

Example cont.

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

16

Example

ARTxx

G E

21

One-parameter Margules equation

Page 9: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

17

Example cont.

221ln Ax 2

12ln Ax

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

18

Example cont.

Page 10: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

19

Example

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

20

Page 11: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

21

Example cont.

Set of non-linear equation that should be solved numerically:

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

22

Example cont.

Page 12: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

23

Example cont.

What does

this mean?

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

24

Example

Page 13: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

25

Example cont.

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

26

Example cont.

a) The pressure is the bubble pressure at which the system composition equal the liquid

composition

Page 14: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

27

The value of A is negative

The activity coefficient γ <1.0

o The partial pressure of of component 1 will be less than the value for the case of ideal solution

o The negative A value implies a negative excess Gibbs free energy and hence the liquid phase

component attract each other more than attracting themselves, i.e. stabilizing attraction

o They exhibit net attractive interaction

o It is harder to make the liquid transfer to the vapor phase

Example cont.

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

28

Page 15: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

29

Margules equations

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

30

Van Laar equation

Page 16: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

31

Wilson model

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

32

Wilson model

Page 17: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

33

NRTL model

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

34

NRTL model

Page 18: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

35

NRTL model

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

36

UNIQUAC model

Page 19: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

37

UNIQUAC model

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

38

UNIQUAC model

Page 20: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

39

Group contribution methods

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

40

UNIFAC model

Page 21: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

41

UNIFAC model

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

42

Models for difficult mixtures

Page 22: Lec 7-GE models and VLE data.ppt

Chemical Engineering Department | University of Jordan | Amman 11942, Jordan

Tel. +962 6 535 5000 | 22888

43

Selection of models