Enthelpy-concentration diagram - how to generate.

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SUMMARY

The forum discussion centers on generating an enthalpy-concentration diagram in Excel using Dalton's Law and Raoult's Law. The original poster (OP) encountered issues with intermediate enthalpy values when changing the reference temperature, despite following computations from two referenced academic papers. The OP confirmed that the enthalpy differences for vapor and liquid lines should remain constant regardless of the reference temperature. The issue was resolved through private communication with another forum member, Chet.

PREREQUISITES
  • Understanding of Dalton's Law and Raoult's Law
  • Proficiency in Excel for data analysis and computation
  • Knowledge of thermodynamics, specifically enthalpy concepts
  • Familiarity with vapor-liquid equilibrium (VLE) calculations
NEXT STEPS
  • Research how to implement Dalton's Law in Excel for enthalpy calculations
  • Explore Raoult's Law applications in real-world scenarios
  • Study the impact of reference temperature on thermodynamic properties
  • Learn advanced Excel techniques for creating dynamic diagrams
USEFUL FOR

Chemical engineers, thermodynamics students, and professionals involved in process design and optimization will benefit from this discussion, particularly those working with enthalpy-concentration diagrams and vapor-liquid equilibrium analysis.

maistral
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So I wanted to create an enthalpy-concentration diagram generator in Excel using Dalton's Law and Raoult's Law (ideal stuff).

The problem is with the formulation. I studied and used this .pdf file form a university in HK:
http://ihome.ust.hk/~kexhu/ceng3210/221-05.pdf

Seeing as it also agrees with this paper in SA:
http://faculty.ksu.edu.sa/Emad.Ali/mylib/CHE411/CH3.pdf

I then decided to give it a roll. I managed to do their computations in an Excel spreadsheet with the reference temperature equal to the boiling point of the lighter component.

The problem began to appear when I changed the reference temperature. Changing the reference temperature totally changed the values of the intermediate enthalpies. If I am correct, the difference in enthalpies for the vapor lines and the liquid lines must be constant whatever the reference temperature is. I then backtracked to the previous example by the .pdf files, the computations seem to be correct. The changes in enthalpy for (0,0) and (1,1) of the VLE were held constant, though.

I managed to whip up an Excel spreadsheet for it. I'm hoping you guys could pinpoint what I did wrong, or did I miss something else. And yes, this again wasn't discussed in our undergraduate studies (lol). This is the link for the file:
http://media.angelfire.lycos.com/5684886/2337329.xlsx
 
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I'm sorry you are not generating any responses at the moment. Is there any additional information you can share with us? Any new findings?
 
Greg Bernhardt said:
I'm sorry you are not generating any responses at the moment. Is there any additional information you can share with us? Any new findings?

Hi Greg,

I helped this OP overcome his difficulties in PMs several weeks ago. He contacted me separately via a private message. So this issue is resolved.

Chet
 

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