Journals / Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering / 1988 / Cilt: 34 - Sayı: 01.02

LIMITS ON THE PREDICTION OF İSOBARİC TERNARY PHASE EQUILIBRIA BY NRTL AND LEMF EQUATIONS

Pages
142–158
Publication Date
1899-01-01
DOI
—
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AI Summary & Key Takeaways

AI Insight
⚡ TL;DR(Too Long; Didn't Read)

For physical interaetions about 235 cal/g.mol the NRTL equation was found to be superior in the predietion of ternary VLE data with Standard deviation ranging from 12-17 % whereas the LEMF equation conld predict the ternary vapour phase with in the accuracy of 16-21 %

📌 3 Key Takeaways

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Objective & Hypothesis:The isobaric separation of multicomponent mixtures by distillation reauire reliable vapour- liquid equilibrium data.
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Key Findings & Data:Both equations gave reasonable results fer binary systems with intermolecular interaetions (HE max < 200 cal/g.mol).
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Conclusion & Impact:For physical interaetions about 235 cal/g.mol the NRTL equation was found to be superior in the predietion of ternary VLE data with Standard deviation ranging from 12-17 % whereas the LEMF equation conld predict the ternary vapour phase with in the accuracy of 16-21 %
🔬Design:Research Article
📍Scope:Comprehensive Sample
⚙️Variables:Therefore · A ternary · For physical

Abstract

The isobaric separation of multicomponent mixtures by distillation reauire reliable vapour- liquid equilibrium data. Therefore, the separation is dependent on the predictive thermodyna- mic method used for estimation of vapour-Iiquid equilibria. The abilities of the NRTL and LEMF equations to predict isobaric binary and ternary vapour-liquid equilibria using only two or more lower heats of mixing data were compared. A ternary and three binary systems compri- sing the ternary were studied. Both equations gave reasonable results fer binary systems with intermolecular interaetions (HE max < 200 cal/g.mol). For physical interaetions about 235 cal/g.mol the NRTL equation was found to be superior in the predietion of ternary VLE data with Standard deviation ranging from 12-17 % whereas the LEMF equation conld predict the ternary vapour phase with in the accuracy of 16-21 %

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Cite This Article

ÖZALP, Ü. (1899). LIMITS ON THE PREDICTION OF İSOBARİC TERNARY PHASE EQUILIBRIA BY NRTL AND LEMF EQUATIONS. Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering, Cilt: 34 - Sayı: 01.02, 142–158. https://ajindex.com/articles/827611

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References (1)

  1. Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering