Lec 2 : Classical Thermodynamics of Phase Equilibria
4
Lec 3 : Classical Thermodynamics of Phase Equilibria – 2
5
Lec 4: Thermodynamic Properties from Volumetric Data
6
Lec 5: Fugacity from Volumetric Data - 1
7
Lec 6: Fugacity from Volumetric Data – 2
8
Lec 7: Intermolecular Forces and Non-Ideal Behaviour
9
Lec 8: Intermolecular Forces-Potential Energy Functions
10
Lec 9: Molecular Theory of Corresponding States
11
Lec 10: Molecular Theory of Corresponding States – 2
12
Lec 11: Intermolecular Potential and EoS
13
Lec 12: Virial Coefficients from Potential Functions
14
Lec 13: Virial Coefficients from Corresponding States Theory
15
Lec 14: Fugacities in Gaseous Mixtures
16
Lec 15: Fugacities in Gaseous Mixtures - 2
17
Lec 16: Fugacities in Gaseous Mixtures - 3
18
Lec 17: Liquid Mixtures and Excess Functions
19
Lec 18: Excess Functions and Activity Coefficients
20
Lec 19: Activity Coefficients and Thermodynamic Consistency
21
Lec 20: Models for Excess Gibbs Energy
22
Lec 21: Models for Excess Gibbs Energy - 2
23
Lec 22: Models for Excess Gibbs Energy - 3
24
Lec 23: Vapour - Liquid Equilibrium
25
Lec 24: Vapour - Liquid Equilibrium - 2
26
Lec 25: Vapour - Liquid Equilibrium - 3
27
Lec 26: Liquid - Liquid Equilibrium
28
Lec 27: Liquid - Liquid Equilibrium - 2
29
Lec 28: Vapour - Liquid - Liquid Equilibrium
30
Lec 29: Vapour - Liquid - Liquid Equilibrium - 2
31
Lec 30: Solid - Liquid Equilibrium
32
Lec 31: Solid - Liquid Equilibrium - 2
Description:
COURSE OUTLINE: In any chemical process, often one encounter interaction between phases where the transfer of species takes place from one phase to other. There exists several situations of vapor-liquid, liquid-liquid, vapor-liquid-liquid, solid-liquid equilibria in chemical engineering processes. Often these situations are dealt with assumption of ideal behavior and binary systems but in reality non-ideality and multicomponent mixtures exists and accordingly one has to deal with such situations. This course offers step-by-step understanding of required thermodynamic properties to handle such equilibrium cases and explore possible ways of solving problems associated with non-ideality in VLE, LLE, VLLE and SLE for multicomponent mixtures.