Experimental and modelling of the vapor-liquid equilibria of [Cnmim]Br(n = 2, 3, 4) + H2O systems

•Vapor-liquid equilibrium (VLE) data of the three binary systems of [Cnmim]Br + H2O (n = 2, 3, 4) have been measured.•The NRTL and e-NRTL models can be well used for calculation of the investigated systems and the absolute average relative deviations (AARD %) are 2.69% and 2.97%.•The imidazolium-bas...

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Published inFluid phase equilibria Vol. 565; p. 113654
Main Authors Guo, Yicang, Cao, Jinxiang, Wang, Fang, Ding, Yan, Li, Jinlong, Paricaud, Patrice
Format Journal Article
LanguageEnglish
Published Elsevier B.V 01.02.2023
Elsevier
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Abstract •Vapor-liquid equilibrium (VLE) data of the three binary systems of [Cnmim]Br + H2O (n = 2, 3, 4) have been measured.•The NRTL and e-NRTL models can be well used for calculation of the investigated systems and the absolute average relative deviations (AARD %) are 2.69% and 2.97%.•The imidazolium-based ILs proposed in this work can dramatically reduce the saturated vapor pressure of pure water, have the potential to be working pairs. Mixtures of ionic liquids (ILs) and water are considered as promising working pair fluids for absorption refrigeration systems (ARS), and they have been the subject of intensive research in recent years. The performance of these mixtures as working fluids directly depends on the phase behavior and thermodynamic properties. In this work, the vapor-liquid equilibrium (VLE) data of three binary systems of 1-ethyl-3-methylimidazolium bromide and water ([C2mim]Br + H2O), 1-propyl-3-methylimidazolium bromide and water ([C3mim]Br + H2O) and 1-buthyl-3-methylimidazolium bromide and water ([C4mim]Br + H2O) have been measured by using the boiling method at pressures ranging from 7.96kPa to 50.10kPa and mole fractions of ILs ranging from 0.02 to 0.50. The thermodynamic models NRTL and e-NRTL are used to correlate the experimental data and a good agreement between the models and the data is obtained. It is found from VLE data that the addition of ILs in water leads to a dramatic decrease of the saturated vapor pressure of the system, and the systems exhibit a high deviation from Raoult's law. Therefore, the three IL + water binary systems have a great potential as working pairs for ARS. In addition, shorter alkyl chains of the IL cation leads to a stronger ability ([C2mim]Br+ > [C3mim]Br+ > [C4mim]Br+) to absorb water.
AbstractList •Vapor-liquid equilibrium (VLE) data of the three binary systems of [Cnmim]Br + H2O (n = 2, 3, 4) have been measured.•The NRTL and e-NRTL models can be well used for calculation of the investigated systems and the absolute average relative deviations (AARD %) are 2.69% and 2.97%.•The imidazolium-based ILs proposed in this work can dramatically reduce the saturated vapor pressure of pure water, have the potential to be working pairs. Mixtures of ionic liquids (ILs) and water are considered as promising working pair fluids for absorption refrigeration systems (ARS), and they have been the subject of intensive research in recent years. The performance of these mixtures as working fluids directly depends on the phase behavior and thermodynamic properties. In this work, the vapor-liquid equilibrium (VLE) data of three binary systems of 1-ethyl-3-methylimidazolium bromide and water ([C2mim]Br + H2O), 1-propyl-3-methylimidazolium bromide and water ([C3mim]Br + H2O) and 1-buthyl-3-methylimidazolium bromide and water ([C4mim]Br + H2O) have been measured by using the boiling method at pressures ranging from 7.96kPa to 50.10kPa and mole fractions of ILs ranging from 0.02 to 0.50. The thermodynamic models NRTL and e-NRTL are used to correlate the experimental data and a good agreement between the models and the data is obtained. It is found from VLE data that the addition of ILs in water leads to a dramatic decrease of the saturated vapor pressure of the system, and the systems exhibit a high deviation from Raoult's law. Therefore, the three IL + water binary systems have a great potential as working pairs for ARS. In addition, shorter alkyl chains of the IL cation leads to a stronger ability ([C2mim]Br+ > [C3mim]Br+ > [C4mim]Br+) to absorb water.
ArticleNumber 113654
Author Cao, Jinxiang
Ding, Yan
Li, Jinlong
Paricaud, Patrice
Wang, Fang
Guo, Yicang
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Keywords Ionic liquids
NRTL
Vapor-liquid equilibrium
Working fluid
e-NRTL
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Snippet •Vapor-liquid equilibrium (VLE) data of the three binary systems of [Cnmim]Br + H2O (n = 2, 3, 4) have been measured.•The NRTL and e-NRTL models can be well...
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StartPage 113654
SubjectTerms Chemical engineering
Chemical Sciences
e-NRTL
Ionic liquids
NRTL
Vapor-liquid equilibrium
Working fluid
Title Experimental and modelling of the vapor-liquid equilibria of [Cnmim]Br(n = 2, 3, 4) + H2O systems
URI https://dx.doi.org/10.1016/j.fluid.2022.113654
https://ensta-paris.hal.science/hal-04208022
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