lec 7-ge models and vle data.ppt
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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
GE models and VLE data
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
Tel. +962 6 535 5000 | 22888
2
Review
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
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Determination of GE from Experimental Data
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Determination of GE from Experimental Data
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example
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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
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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
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
For binary mixture
Then get
at known x1, x2 and
Show this
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Example cont.
Then
At the given conditions:
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Example cont.
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
Unknowns,
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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What does this mean?
Example cont.
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Example
ARTxx
G E
21
One-parameter Margules equation
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
221ln Ax 2
12ln Ax
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
Tel. +962 6 535 5000 | 22888
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Example
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Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
Set of non-linear equation that should be solved numerically:
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Example cont.
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
Tel. +962 6 535 5000 | 22888
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Example cont.
What does
this mean?
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
Tel. +962 6 535 5000 | 22888
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Example
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Example cont.
a) The pressure is the bubble pressure at which the system composition equal the liquid
composition
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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.
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Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Margules equations
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Van Laar equation
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Wilson model
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Wilson model
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NRTL model
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NRTL model
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NRTL model
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UNIQUAC model
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UNIQUAC model
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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UNIQUAC model
Chemical Engineering Department | University of Jordan | Amman 11942, Jordan
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Group contribution methods
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UNIFAC model
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UNIFAC model
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Models for difficult mixtures
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Selection of models