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C = 2 Gibbs phase rule F = C – P + 2 Pressure Temp. Comp. xA F = 3

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Presentation on theme: "C = 2 Gibbs phase rule F = C – P + 2 Pressure Temp. Comp. xA F = 3"— Presentation transcript:

1 C = 2 Gibbs phase rule F = C – P + 2 Pressure Temp. Comp. xA F = 3

2 Partial molar quantities

3 Thermodynamics of ideal mixing gases/liquids

4 Thermodynamics of mixing liquids
Ideal mixing (Raoult)

5 Thermodynamics of mixing liquids
Non-ideal mixing

6

7 Vapour liquid diagrams
Ideal solution (Raoult)

8 Vapour liquid diagrams
Ideal solution (Raoult)

9 Vapour pressure diagrams
C = 2 Vapour pressure diagrams Ideal solution

10 Vapour pressure diagrams
C = 2 Vapour pressure diagrams Ideal solution

11 Vapour pressure diagrams
C = 2 Vapour pressure diagrams Ideal solution

12 Vapour pressure diagrams
C = 2 Vapour pressure diagrams Ideal solution

13 Vapour pressure diagrams
C = 2 Vapour pressure diagrams Fixed T P = 1 P = 2 F’ = C – P + 1 F = C – P + 2 P = 1 Ideal solution

14 { C = 2 Lever rule Isopleth Tie line P = 1 P = 2 Lever rule P = 1
Phase α Type equation here. P = 1 P = 2 𝑙 β 𝑙 α 𝑛 α 𝑙 α = 𝑛 β 𝑙 β Phase β Lever rule P = 1

15

16 Pressure-composition diagrams
F = 3 F = 0 F = 1 Temp. F = 2 Comp. xA Temperature-composition diagrams

17 Pressure-composition diagrams
Fixed T Pressure F = 3 F = 0 F = 1 Temp. F = 2 Comp. xA

18 Temperature-composition diagrams
Pressure F = 3 F = 0 F = 1 Temp. Fixed P F = 2 Comp. xA Temperature-composition diagrams

19 Pressure-composition diagrams
Ideal solution Fixed T

20 Temperature-composition diagrams
Ideal solution P = 1 P = 2 (Clapeyron) P = 1 F = C – P + 2 Fixed P F’ = C – P + 1

21 Temperature-composition diagrams
vapour GE = 0 liquid GE < 0

22 Temperature-composition diagrams
GE >> 0 vapour GE = 0 liquid Non-ideal solutions GE < 0 GE << 0

23 Temperature-composition diagrams
GE >> 0 Non-ideal solutions vapour GE = 0 liquid GE < 0 GE << 0

24 Temperature-composition diagrams
vapour P = 1 P = 2 P = 1 vapour liquid P = 2 liquid P = 2 P = 1 Low boiling azeotrope High boiling azeotrope H2O/Eth: 4 78°C H2O/HCl: °C

25 Impossible azeotropes
C = 2 Impossible azeotropes would lead to g-g separation

26

27 Cl4ethene/cyclopentene
{ Non-ideal mixing (Excess functions) Benzene/cyclohexane Ideal Regular Quasi regular SE =0 ≠0 HE Cl4ethene/cyclopentene

28 Regular solution -T = (Regular solution: HE ≠ 0)
(Regular solution: SE = 0)

29 Regular solution -T = (Regular solution: HE ≠ 0)

30 Regular solution -T = (Regular solution: HE ≠ 0)
(Regular solution: SE = 0)

31 Regular solution -T = (Regular solution: HE ≠ 0)
(Regular solution: SE = 0)

32 Liquid-liquid separation for Regular solution


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