The Experts below are selected from a list of 246 Experts worldwide ranked by ideXlab platform
Isabel Vidal - One of the best experts on this subject based on the ideXlab platform.
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liquid liquid equilibria of the ternary mixtures water propanoic acid MEthyl Ethyl Ketone and water propanoic acid MEthyl propyl Ketone
Journal of Chemical & Engineering Data, 1995Co-Authors: Alberto Arce, Antonio Blanco, Pilar Souza, Isabel VidalAbstract:We report mutual solubilities of water+MEthyl Ethyl Ketone and water+MEthyl propyl Ketone at temperatures between 25 and 55 o C, and binodal curves and liquid-liquid equilibria for water+propanoic acid+MEthyl Ethyl Ketone and water+propanoic acid+MEthyl propyl Ketone in the same temperature range. UNIQUAC equations fitted the experimental data better than NRTL equations: the average rms phase composition error was 0.2% for UNIQUAC as compared to 0.3% for RNTL, and the rms relative error in the solute distribution ratio was 5% for UNIQUAC as compared to 7.5% for RNTL
Alberto Arce - One of the best experts on this subject based on the ideXlab platform.
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liquid liquid equilibria of the ternary mixtures water propanoic acid MEthyl Ethyl Ketone and water propanoic acid MEthyl propyl Ketone
Journal of Chemical & Engineering Data, 1995Co-Authors: Alberto Arce, Antonio Blanco, Pilar Souza, Isabel VidalAbstract:We report mutual solubilities of water+MEthyl Ethyl Ketone and water+MEthyl propyl Ketone at temperatures between 25 and 55 o C, and binodal curves and liquid-liquid equilibria for water+propanoic acid+MEthyl Ethyl Ketone and water+propanoic acid+MEthyl propyl Ketone in the same temperature range. UNIQUAC equations fitted the experimental data better than NRTL equations: the average rms phase composition error was 0.2% for UNIQUAC as compared to 0.3% for RNTL, and the rms relative error in the solute distribution ratio was 5% for UNIQUAC as compared to 7.5% for RNTL
Antonio Blanco - One of the best experts on this subject based on the ideXlab platform.
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liquid liquid equilibria of the ternary mixtures water propanoic acid MEthyl Ethyl Ketone and water propanoic acid MEthyl propyl Ketone
Journal of Chemical & Engineering Data, 1995Co-Authors: Alberto Arce, Antonio Blanco, Pilar Souza, Isabel VidalAbstract:We report mutual solubilities of water+MEthyl Ethyl Ketone and water+MEthyl propyl Ketone at temperatures between 25 and 55 o C, and binodal curves and liquid-liquid equilibria for water+propanoic acid+MEthyl Ethyl Ketone and water+propanoic acid+MEthyl propyl Ketone in the same temperature range. UNIQUAC equations fitted the experimental data better than NRTL equations: the average rms phase composition error was 0.2% for UNIQUAC as compared to 0.3% for RNTL, and the rms relative error in the solute distribution ratio was 5% for UNIQUAC as compared to 7.5% for RNTL
Pilar Souza - One of the best experts on this subject based on the ideXlab platform.
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liquid liquid equilibria of the ternary mixtures water propanoic acid MEthyl Ethyl Ketone and water propanoic acid MEthyl propyl Ketone
Journal of Chemical & Engineering Data, 1995Co-Authors: Alberto Arce, Antonio Blanco, Pilar Souza, Isabel VidalAbstract:We report mutual solubilities of water+MEthyl Ethyl Ketone and water+MEthyl propyl Ketone at temperatures between 25 and 55 o C, and binodal curves and liquid-liquid equilibria for water+propanoic acid+MEthyl Ethyl Ketone and water+propanoic acid+MEthyl propyl Ketone in the same temperature range. UNIQUAC equations fitted the experimental data better than NRTL equations: the average rms phase composition error was 0.2% for UNIQUAC as compared to 0.3% for RNTL, and the rms relative error in the solute distribution ratio was 5% for UNIQUAC as compared to 7.5% for RNTL
Francisco Ruiz - One of the best experts on this subject based on the ideXlab platform.
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Isobaric vapor-liquid equilibria for the binary system 2-propanol + MEthyl Ethyl Ketone and for the ternary system 1-butanol + 2-propanol + MEthyl Ethyl Ketone at 101.3 kPa
Journal of Chemical & Engineering Data, 2002Co-Authors: Maria Del Mar Olaya, Vicente Gomis, And Julia Moltó, Francisco RuizAbstract:Isobaric vapor−liquid equilibrium data have been measured for the 2-propanol + MEthyl Ethyl Ketone binary system and for the 1-butanol + 2-propanol + MEthyl Ethyl Ketone ternary system at 101.3 kPa in a temperature range from 351 to 382 K. The data were found to be thermodynamically consistent according to the point to point L−W method of Wisniak. The equilibrium data were correlated using Wilson, NRTL, and UNIQUAC models for which the parameters are reported.