Liquid–liquid equilibria for ethyl esters+ethanol+water systems: Experimental measurements and CPA EoS modeling
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João A. P. Coutinho | Eduardo A. C. Batista | Luis A. Follegatti-Romero | Antonio J. A. Meirelles | Mariana B. Oliveira
[1] D. L. Reece,et al. TWO-YEAR STORAGE STUDY WITH METHYL AND ETHYL ESTERS OF RAPESEED , 1998 .
[2] João A. P. Coutinho,et al. Liquid–liquid equilibria for ternary systems containing ethyl esters, ethanol and glycerol at 323.15 and 353.15 K , 2012 .
[3] J. Arauzo,et al. Water Cleaning of Biodiesel. Effect of Catalyst Concentration, Water Amount, and Washing Temperature on Biodiesel Obtained from Rapeseed Oil and Used Oil , 2010 .
[4] A. Marcilla,et al. Liquid–liquid–solid equilibria for the quaternary system water+ethanol+1-pentanol+sodium chloride at 25°C , 1995 .
[5] E. Batista,et al. Mutual Solubility of Pseudobinary Systems Containing Vegetable Oils and Anhydrous Ethanol from (298.15 to 333.15) K , 2010 .
[6] J. F. González,et al. Biodiesel Fuels from Vegetable Oils: Transesterification of Cynara cardunculus L. Oils with Ethanol , 2002 .
[7] J. Coutinho,et al. Phase Equilibria of Ester + Alcohol Systems and Their Description with the Cubic-Plus-Association Equation of State , 2010 .
[8] M. Sharma,et al. Prospects of biodiesel production from vegetable oils in India , 2005 .
[9] João A. P. Coutinho,et al. Modeling of Biodiesel Multicomponent Systems with the Cubic-Plus-Association (CPA) Equation of State , 2010 .
[10] I. Marrucho,et al. Modeling the Liquid−Liquid Equilibria of Water + Fluorocarbons with the Cubic-Plus-Association Equation of State , 2007 .
[11] B. Moser. Biodiesel production, properties, and feedstocks , 2009, In Vitro Cellular & Developmental Biology - Plant.
[12] João A. P. Coutinho,et al. Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters , 2010 .
[13] E. Nikitin,et al. Critical properties of long-chain substances from the hypothesis of functional self-similarity , 2005 .
[14] J. Coutinho,et al. Modeling Phase Equilibria Relevant to Biodiesel Production: A Comparison of gE Models, Cubic EoS, EoS−gE and Association EoS , 2011 .
[15] Mario R. Meneghetti,et al. Biodiesel from Castor Oil: A Comparison of Ethanolysis versus Methanolysis , 2006 .
[16] E. Voutsas,et al. Water/Hydrocarbon Phase Equilibria Using the Thermodynamic Perturbation Theory , 2000 .
[17] L. C. Meher,et al. Technical aspects of biodiesel production by transesterification—a review , 2006 .
[18] Antonio J. A. Meirelles,et al. Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry , 2011 .
[19] R. L. Skelton,et al. Comparison of purification methods for biodiesel , 2008 .
[20] João A. P. Coutinho,et al. Prediction of cloud points of biodiesel , 2008 .
[21] António J. Queimada,et al. Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State , 2009 .
[22] G. Kontogeorgis,et al. Multicomponent phase equilibrium calculations for water–methanol–alkane mixtures , 1999 .
[23] E. Voutsas,et al. Prediction of phase equilibria in water/alcohol/alkane systems , 1999 .
[24] I. M. Atadashi,et al. Biodiesel separation and purification: A review , 2011 .
[25] Ultrasonic Comparative Assessment for Biodiesel Production from Rapeseed , 2010 .
[26] Michael L. Michelsen,et al. Physical properties from association models , 2001 .
[27] Y. Basiron. Palm oil production through sustainable plantations , 2007 .
[28] I. Marrucho,et al. Surface tension of chain molecules through a combination of the gradient theory with the CPA EoS , 2008 .
[29] Dimitrios P. Tassios,et al. An Equation of State for Associating Fluids , 1996 .
[30] João A. P. Coutinho,et al. Mutual solubilities of hydrocarbons and water with the CPA EoS , 2007 .
[31] M. Michelsen,et al. Application of the Cubic-Plus-Association (CPA) Equation of State to Complex Mixtures with Aromatic Hydrocarbons , 2006 .
[32] E. Batista,et al. Liquid−Liquid Equilibrium for Ternary Systems Containing Ethyl Esters, Anhydrous Ethanol and Water at 298.15, 313.15, and 333.15 K , 2010 .
[33] Liquid–Liquid Equilibrium Data for Reactional Systems of Ethanolysis at 298.3 K , 2008 .
[34] João A. P. Coutinho,et al. Prediction of near and supercritical fatty acid ester + alcohol systems with the CPA EoS , 2010 .
[35] Olivera S. Stamenković,et al. Kinetics of the base-catalyzed sunflower oil ethanolysis , 2010 .
[36] Liquid-Liquid Equilibrium for Ternary Systems Containing Ethyl Esters , Anhydrous Ethanol and Water at 298 , 2010 .
[37] Renzo Di Felice,et al. Component Distribution between Light and Heavy Phases in Biodiesel Processes , 2008 .
[38] Shin-ichi Sakai,et al. Application of UNIFAC models for prediction of vapor–liquid and liquid–liquid equilibria relevant to separation and purification processes of crude biodiesel fuel , 2009 .
[39] Stanley H. Huang,et al. Equation of state for small, large, polydisperse, and associating molecules , 1990 .
[40] J. Prausnitz,et al. Phase Equilibria for Systems Containing Hydrocarbons, Water, and Salt: An Extended Peng−Robinson Equation of State , 1998 .
[41] Erich A. Müller,et al. Molecular-Based Equations of State for Associating Fluids: A Review of SAFT and Related Approaches , 2001 .
[42] I. Marrucho,et al. Description of the mutual solubilities of fatty acids and water with the CPA EoS , 2009 .
[43] João A. P. Coutinho,et al. Liquid–liquid equilibria for the canola oil biodiesel + ethanol + glycerol system , 2011 .
[44] M. Michelsen,et al. Application of the Cubic-Plus-Association (CPA) Equation of State to Cross-Associating Systems , 2005 .
[45] João A. P. Coutinho,et al. Liquid – liquid equilibria for ternary systems containing ethyl esters , ethanol and glycerol at 323 . 15 and 353 . 15 , 2012 .
[46] João A. P. Coutinho,et al. Prediction of Water Solubility in Biodiesel with the CPA Equation of State , 2008 .