The Experts below are selected from a list of 18537 Experts worldwide ranked by ideXlab platform
Inmaculada Blasco - One of the best experts on this subject based on the ideXlab platform.
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Study of the LLE, VLE, and VLLE of the Ternary System Water + 1-Butanol + Isoamyl Alcohol at 101.3 kPa
Journal of Chemical & Engineering Data, 2018Co-Authors: María Dolores Saquete, Alicia Font, Jorge Garcia-cano, Inmaculada BlascoAbstract:The liquid–liquid equilibrium of the water + 1-butanol + Isoamyl Alcohol system at 303.15 and 313.15 K has been determined experimentally. The UNIQUAC, NRTL, and UNIFAC models have been employed to correlate and predict liquid–liquid equilibria (LLE) and compare them with the experimental data. Additionally, the vapor–liquid and vapor–liquid–liquid equilibria (VLE and VLLE, respectively) of this system have been determined using a modified Fischer LABODEST still. The data obtained have been used to correlate and obtain the binary interaction parameters for UNIQUAC and NRTL. The validity of the models to reproduce the VLE and VLLE data has been analyzed.
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study of the lle vle and vlle of the ternary system water 1 butanol Isoamyl Alcohol at 101 3 kpa
Journal of Chemical & Engineering Data, 2018Co-Authors: María Dolores Saquete, Alicia Font, Jorge Garciacano, Inmaculada BlascoAbstract:The liquid–liquid equilibrium of the water + 1-butanol + Isoamyl Alcohol system at 303.15 and 313.15 K has been determined experimentally. The UNIQUAC, NRTL, and UNIFAC models have been employed to correlate and predict liquid–liquid equilibria (LLE) and compare them with the experimental data. Additionally, the vapor–liquid and vapor–liquid–liquid equilibria (VLE and VLLE, respectively) of this system have been determined using a modified Fischer LABODEST still. The data obtained have been used to correlate and obtain the binary interaction parameters for UNIQUAC and NRTL. The validity of the models to reproduce the VLE and VLLE data has been analyzed.
Mehmet Bilgin - One of the best experts on this subject based on the ideXlab platform.
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Liquid Phase Equilibria for Mixtures of (Water + Morpholine + Ethyl Nonanoate, Dimethyl Phthalate, or Isoamyl Alcohol) at 298.15 K
Journal of Chemical & Engineering Data, 2010Co-Authors: Lutfullah M. Sevgili, Mehmet Bilgin, Selin ŞahinAbstract:This work reports liquid−liquid equilibrium (LLE) data for the mixtures {water (1) + morpholine (2) + ethyl nonanoate, dimethyl phthalate, or Isoamyl Alcohol (3)} at 298.15 K and 101.3 kPa. The solubility curves and tie-line end compositions were examined for the related mixtures. The reliability of the experimental tie-line data was verified by using the Othmer−Tobias correlation. Distribution coefficients and separation factors were evaluated for the immiscibility region. Although all of the proposed solvents show low distribution coefficients, they can be served as convenient agents for extracting morpholine from aqueous medium, since they exhibit high separation factors. The experimental tie-line data were correlated by universal quasichemical activity coefficient (UNIQUAC) model representing the LLE data for these systems with respect to tie-line slopes only.
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liquid phase equilibria for mixtures of water morpholine ethyl nonanoate dimethyl phthalate or Isoamyl Alcohol at 298 15 k
Journal of Chemical & Engineering Data, 2010Co-Authors: Lutfullah M. Sevgili, Mehmet Bilgin, Selin ŞahinAbstract:This work reports liquid−liquid equilibrium (LLE) data for the mixtures {water (1) + morpholine (2) + ethyl nonanoate, dimethyl phthalate, or Isoamyl Alcohol (3)} at 298.15 K and 101.3 kPa. The solubility curves and tie-line end compositions were examined for the related mixtures. The reliability of the experimental tie-line data was verified by using the Othmer−Tobias correlation. Distribution coefficients and separation factors were evaluated for the immiscibility region. Although all of the proposed solvents show low distribution coefficients, they can be served as convenient agents for extracting morpholine from aqueous medium, since they exhibit high separation factors. The experimental tie-line data were correlated by universal quasichemical activity coefficient (UNIQUAC) model representing the LLE data for these systems with respect to tie-line slopes only.
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liquid liquid equilibria of water butyric acid Isoamyl Alcohol ternary system
The Journal of Chemical Thermodynamics, 2005Co-Authors: Mehmet Bilgin, Ş. İsmail Kırbaşlar, Önder Özcan, Umur DramurAbstract:Abstract (Liquid + liquid) equilibrium (LLE) data for the ternary system (water + butyric acid + Isoamyl Alcohol) have been determined experimentally at T = (298.15, 308.15 and 318.15) K. Complete phase diagrams were obtained by determining solubility and the tie-line data. Tie-line compositions were correlated by Othmer–Tobias method. The UNIFAC method was used to predict the phase equilibrium in the system using the interaction parameters determined from experimental data between groups CH3, CH2, CH, COOH, OH and H2O. It is found that UNIFAC group interaction parameters used for LLE could not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region.
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(liquid + liquid) equilibria of (water + butyric acid + Isoamyl Alcohol) ternary system
The Journal of Chemical Thermodynamics, 2005Co-Authors: Mehmet Bilgin, Ş. İsmail Kırbaşlar, Önder Özcan, Umur DramurAbstract:Abstract (Liquid + liquid) equilibrium (LLE) data for the ternary system (water + butyric acid + Isoamyl Alcohol) have been determined experimentally at T = (298.15, 308.15 and 318.15) K. Complete phase diagrams were obtained by determining solubility and the tie-line data. Tie-line compositions were correlated by Othmer–Tobias method. The UNIFAC method was used to predict the phase equilibrium in the system using the interaction parameters determined from experimental data between groups CH3, CH2, CH, COOH, OH and H2O. It is found that UNIFAC group interaction parameters used for LLE could not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region.
María Dolores Saquete - One of the best experts on this subject based on the ideXlab platform.
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Study of the LLE, VLE, and VLLE of the Ternary System Water + 1-Butanol + Isoamyl Alcohol at 101.3 kPa
Journal of Chemical & Engineering Data, 2018Co-Authors: María Dolores Saquete, Alicia Font, Jorge Garcia-cano, Inmaculada BlascoAbstract:The liquid–liquid equilibrium of the water + 1-butanol + Isoamyl Alcohol system at 303.15 and 313.15 K has been determined experimentally. The UNIQUAC, NRTL, and UNIFAC models have been employed to correlate and predict liquid–liquid equilibria (LLE) and compare them with the experimental data. Additionally, the vapor–liquid and vapor–liquid–liquid equilibria (VLE and VLLE, respectively) of this system have been determined using a modified Fischer LABODEST still. The data obtained have been used to correlate and obtain the binary interaction parameters for UNIQUAC and NRTL. The validity of the models to reproduce the VLE and VLLE data has been analyzed.
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study of the lle vle and vlle of the ternary system water 1 butanol Isoamyl Alcohol at 101 3 kpa
Journal of Chemical & Engineering Data, 2018Co-Authors: María Dolores Saquete, Alicia Font, Jorge Garciacano, Inmaculada BlascoAbstract:The liquid–liquid equilibrium of the water + 1-butanol + Isoamyl Alcohol system at 303.15 and 313.15 K has been determined experimentally. The UNIQUAC, NRTL, and UNIFAC models have been employed to correlate and predict liquid–liquid equilibria (LLE) and compare them with the experimental data. Additionally, the vapor–liquid and vapor–liquid–liquid equilibria (VLE and VLLE, respectively) of this system have been determined using a modified Fischer LABODEST still. The data obtained have been used to correlate and obtain the binary interaction parameters for UNIQUAC and NRTL. The validity of the models to reproduce the VLE and VLLE data has been analyzed.
Umur Dramur - One of the best experts on this subject based on the ideXlab platform.
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liquid liquid equilibria of water butyric acid Isoamyl Alcohol ternary system
The Journal of Chemical Thermodynamics, 2005Co-Authors: Mehmet Bilgin, Ş. İsmail Kırbaşlar, Önder Özcan, Umur DramurAbstract:Abstract (Liquid + liquid) equilibrium (LLE) data for the ternary system (water + butyric acid + Isoamyl Alcohol) have been determined experimentally at T = (298.15, 308.15 and 318.15) K. Complete phase diagrams were obtained by determining solubility and the tie-line data. Tie-line compositions were correlated by Othmer–Tobias method. The UNIFAC method was used to predict the phase equilibrium in the system using the interaction parameters determined from experimental data between groups CH3, CH2, CH, COOH, OH and H2O. It is found that UNIFAC group interaction parameters used for LLE could not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region.
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(liquid + liquid) equilibria of (water + butyric acid + Isoamyl Alcohol) ternary system
The Journal of Chemical Thermodynamics, 2005Co-Authors: Mehmet Bilgin, Ş. İsmail Kırbaşlar, Önder Özcan, Umur DramurAbstract:Abstract (Liquid + liquid) equilibrium (LLE) data for the ternary system (water + butyric acid + Isoamyl Alcohol) have been determined experimentally at T = (298.15, 308.15 and 318.15) K. Complete phase diagrams were obtained by determining solubility and the tie-line data. Tie-line compositions were correlated by Othmer–Tobias method. The UNIFAC method was used to predict the phase equilibrium in the system using the interaction parameters determined from experimental data between groups CH3, CH2, CH, COOH, OH and H2O. It is found that UNIFAC group interaction parameters used for LLE could not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region.
Alicia Font - One of the best experts on this subject based on the ideXlab platform.
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Study of the LLE, VLE, and VLLE of the Ternary System Water + 1-Butanol + Isoamyl Alcohol at 101.3 kPa
Journal of Chemical & Engineering Data, 2018Co-Authors: María Dolores Saquete, Alicia Font, Jorge Garcia-cano, Inmaculada BlascoAbstract:The liquid–liquid equilibrium of the water + 1-butanol + Isoamyl Alcohol system at 303.15 and 313.15 K has been determined experimentally. The UNIQUAC, NRTL, and UNIFAC models have been employed to correlate and predict liquid–liquid equilibria (LLE) and compare them with the experimental data. Additionally, the vapor–liquid and vapor–liquid–liquid equilibria (VLE and VLLE, respectively) of this system have been determined using a modified Fischer LABODEST still. The data obtained have been used to correlate and obtain the binary interaction parameters for UNIQUAC and NRTL. The validity of the models to reproduce the VLE and VLLE data has been analyzed.
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study of the lle vle and vlle of the ternary system water 1 butanol Isoamyl Alcohol at 101 3 kpa
Journal of Chemical & Engineering Data, 2018Co-Authors: María Dolores Saquete, Alicia Font, Jorge Garciacano, Inmaculada BlascoAbstract:The liquid–liquid equilibrium of the water + 1-butanol + Isoamyl Alcohol system at 303.15 and 313.15 K has been determined experimentally. The UNIQUAC, NRTL, and UNIFAC models have been employed to correlate and predict liquid–liquid equilibria (LLE) and compare them with the experimental data. Additionally, the vapor–liquid and vapor–liquid–liquid equilibria (VLE and VLLE, respectively) of this system have been determined using a modified Fischer LABODEST still. The data obtained have been used to correlate and obtain the binary interaction parameters for UNIQUAC and NRTL. The validity of the models to reproduce the VLE and VLLE data has been analyzed.
