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Liquid - liquid equilibrium for ternary systems containing ethyl esters, anhydrous ethanol and water at 298.15, 313.15, and 333.15 K / Luis A. Follegatti-Romero in Industrial & engineering chemistry research, Vol. 49 N° 24 (Décembre 2010) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 49 N° 24 (Décembre 2010) . - pp. 12613–12619 Titre : Liquid - liquid equilibrium for ternary systems containing ethyl esters, anhydrous ethanol and water at 298.15, 313.15, and 333.15 K Type de document : texte imprimé Auteurs : Luis A. Follegatti-Romero, Auteur ; Marcelo Lanza, Auteur ; Fabio R. M. Batista, Auteur Année de publication : 2011 Article en page(s) : pp. 12613–12619 Note générale : Chimie industrielle Langues : Anglais (eng) Mots-clés : Ternary  system  Phase  equilibrium  Liquid  liquid  equilibrium Résumé : The most common method used for purifying biodiesel is washing with water. During the biodiesel washing process, two phases are formed, a water-rich phase and an ester-rich one. For this reason, knowledge of the corresponding phase equilibrium is an important step in optimizing the final purification of biodiesel. The objective of this work was to investigate the liquid−liquid equilibrium related to some esters of interest in the production of ethylic biodiesel, in particular the equilibrium data for systems containing ethyl laurate/ethyl myristate + ethanol + water at 298.15, 313.15, and 333.15 K. The data obtained were correlated with the cubic-plus-association equation of state (CPA EoS). It was shown that this model was able to provide a very good description of the phase diagrams of the systems studied. DEWEY : 660 ISSN : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=23692017 [article] Liquid - liquid equilibrium for ternary systems containing ethyl esters, anhydrous ethanol and water at 298.15, 313.15, and 333.15 K [texte imprimé] / Luis A. Follegatti-Romero, Auteur ; Marcelo Lanza, Auteur ; Fabio R. M. Batista, Auteur . - 2011 . - pp. 12613–12619. Chimie industrielle Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 49 N° 24 (Décembre 2010) . - pp. 12613–12619 Mots-clés : Ternary  system  Phase  equilibrium  Liquid  liquid  equilibrium Résumé : The most common method used for purifying biodiesel is washing with water. During the biodiesel washing process, two phases are formed, a water-rich phase and an ester-rich one. For this reason, knowledge of the corresponding phase equilibrium is an important step in optimizing the final purification of biodiesel. The objective of this work was to investigate the liquid−liquid equilibrium related to some esters of interest in the production of ethylic biodiesel, in particular the equilibrium data for systems containing ethyl laurate/ethyl myristate + ethanol + water at 298.15, 313.15, and 333.15 K. The data obtained were correlated with the cubic-plus-association equation of state (CPA EoS). It was shown that this model was able to provide a very good description of the phase diagrams of the systems studied. DEWEY : 660 ISSN : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=23692017