Thermodynamic Behavior of the Phase Equilibrium of Ethyl Acetate + Ethanol + Water Systems at Atmospheric Pressure: Experiment and Modeling (2020)
- Authors:
- USP affiliated authors: SOUSA, MARIVONE NUNHO - EEL ; CASTILLO, PEDRO FELIPE ARCE - EEL ; LOURENÇO, NATALIA INACIO - EEL ; IGARASHI, EDSON MASSAKAZU DE SOUZA - EEL
- Unidade: EEL
- DOI: 10.1021/acs.jced.9b00785
- Subjects: EQUILÍBRIO; SOLUÇÕES AQUOSAS
- Keywords: Ethyl groups; Solution chemistry,
- Agências de fomento:
- Language: Inglês
- Abstract: The fluid phase behavior of liquid–liquid equilibrium (LLE) is an important piece of the separation processes in chemical engineering, mainly for solvent extraction or liquid–liquid extraction. In this work, experimental studies were carried out in the LLE of a ternary system composed of water, ethanol, and ethyl acetate at four different temperatures at atmospheric pressure. A two-step procedure was done for each temperature in the experimental stage. First, the construction of the binodal curve of the ternary system, and second, the determination of the tie-lines (LLE). For the tie-lines, because the configuration of the binodal curve and the refractive index of the liquid phases at equilibrium were known, their compositions were determined. The LLE experimental data were evaluated through the method developed by Marcilla and collaborators. The gamma–gamma approach was used for the modeling, by using the analytical solutions of groups (ASOG), the nonrandom two-liquids (NRTL), and the universal quasichemical (UNIQUAC) models. Results of the thermodynamic modeling were compared with the experimental values, and the deviations of the compositions of the lighter phase were very low for the thermodynamic models used.
- Imprenta:
- Publisher: American Chemical Society (ACS)
- Publisher place: Washington DC
- Date published: 2020
- Source:
- Título: Journal of Chemical & Engineering Data
- ISSN: 0021-9568
- Volume/Número/Paginação/Ano: v.65, n4. , p.1402-1410, 2020
- Este periódico é de assinatura
- Este artigo NÃO é de acesso aberto
- Cor do Acesso Aberto: closed
-
ABNT
ROBLES, Pedro A. et al. Thermodynamic Behavior of the Phase Equilibrium of Ethyl Acetate + Ethanol + Water Systems at Atmospheric Pressure: Experiment and Modeling. Journal of Chemical & Engineering Data, v. 65, p. 1402-1410, 2020Tradução . . Disponível em: https://doi.org/10.1021/acs.jced.9b00785. Acesso em: 06 mar. 2025. -
APA
Robles, P. A., Lourenço, N. I., Igarashi, E. M. de S., Sousa, M. N., & Arce, P. F. (2020). Thermodynamic Behavior of the Phase Equilibrium of Ethyl Acetate + Ethanol + Water Systems at Atmospheric Pressure: Experiment and Modeling. Journal of Chemical & Engineering Data, 65, 1402-1410. doi:10.1021/acs.jced.9b00785 -
NLM
Robles PA, Lourenço NI, Igarashi EM de S, Sousa MN, Arce PF. Thermodynamic Behavior of the Phase Equilibrium of Ethyl Acetate + Ethanol + Water Systems at Atmospheric Pressure: Experiment and Modeling [Internet]. Journal of Chemical & Engineering Data. 2020 ;65 1402-1410.[citado 2025 mar. 06 ] Available from: https://doi.org/10.1021/acs.jced.9b00785 -
Vancouver
Robles PA, Lourenço NI, Igarashi EM de S, Sousa MN, Arce PF. Thermodynamic Behavior of the Phase Equilibrium of Ethyl Acetate + Ethanol + Water Systems at Atmospheric Pressure: Experiment and Modeling [Internet]. Journal of Chemical & Engineering Data. 2020 ;65 1402-1410.[citado 2025 mar. 06 ] Available from: https://doi.org/10.1021/acs.jced.9b00785 - Medição experimental e modelagem termodinâmica do equilíbrio líquido-líquido de sistemas contendo etanol, acetato de etila e água
- Comportamento termodinâmico do equilíbrio líquido-líquido de sistemas ternários à pressão atmosférica: Experimental e modelagem
- Thermodynamic consistency and modeling of high-pressure vapor-liquid equilibrium of light hydrocarbons + ionic liquids systems using the Peng-Robinson Stryjek-Vera equation of state.
- Modelagem e simulação termodinâmica do equilíbrio de fases de sistemas binários contendo componentes do biodiesel a baixas e altas pressões
- Modelagem, consistência e simulação termodinâmica do comportamento de fases líquido-vapor de sistemas binários contendo componentes presentes na produção de biodiesel
- Comportamento termodinâmico do equilíbrio líquido-vapor de sistemas ternários contendo água, metanol e acetona - experimental e modelagem
- Experimental study and thermodynamic modeling of xylitol and sorbitol solubility in mixtures of methanol and ethanol at different temperatures
- Experimental Data and Thermodynamics Modeling (PC-SAFT EoS) of the {CO 2</sub> + Acetone + Pluronic F-127} System at High Pressures
- Experimental data and thermodynamics modeling (PC-SAFT EoS) of the {CO2 + chloroform + PHBV} system at high pressures
- Solubility and Pseudo Polymorphic Behavior of Nicotinic Acid in Alcoholic Solutions: Experimental Data and Phase Equilibrium Modeling
Informações sobre o DOI: 10.1021/acs.jced.9b00785 (Fonte: oaDOI API)
How to cite
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas