The agreement, between the predicted and experimental equilibrium data allows the calculation of isothermal vapour-liquid data for Sys¬tems containing both polar and non-polar compounds.
📌 3 Key Takeaways
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Objective & Hypothesis:The Redlich-Kwong equation of State was used to calculate liquid and vapour phase fuga- cities of Acetic acid (l)-n.
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Key Findings & Data:Heptane (2) and Acetic acid (l)-Benzene (2) Systems for predicting isothermal vapour-Iiquid equilibria.
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Conclusion & Impact:The agreement, between the predicted and experimental equilibrium data allows the calculation of isothermal vapour-liquid data for Sys¬tems containing both polar and non-polar compounds.
🔬Design:Research Article
📍Scope:Comprehensive Sample
⚙️Variables:The Redlich-Kwong · Systems for predicting · non-polar compounds
Abstract
The Redlich-Kwong equation of State was used to calculate liquid and vapour phase fuga- cities of Acetic acid (l)-n. Heptane (2) and Acetic acid (l)-Benzene (2) Systems for predicting isothermal vapour-Iiquid equilibria. The binary interaction coefficients were obtained by a mi- nimization technique with the help of a Computer. The agreement, between the predicted and experimental equilibrium data allows the calculation of isothermal vapour-liquid data for Sys¬tems containing both polar and non-polar compounds.
ÖZALP, Ü. (1899). APPLICATION OF TWO-PARAMETER EOUATION OF STATE TO PREDICTION OF İSOTHERMAL VAPOUR-LIOUID EOUILIBRIA. Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering, Cilt: 34 - Sayı: 01.02, 94–102. https://ajindex.com/articles/827602