2016
DOI: 10.1016/j.molliq.2016.06.107
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Prediction of CO2 solubility in ionic liquids with QM and UNIQUAC models

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Cited by 17 publications
(4 citation statements)
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“…When designing ILs for carbon capture using CAMD, 8 it is important to develop a reliable model for predicting the solubility of CO 2 in ILs. Many traditional thermodynamic or physical models, for example, PHSC state equation, Gibbs–Duhem function, cubic equation of state combined with UNIFAC, COSMO‐RS, and DFT could estimate gas solubility 9–16 . These models could well represent the effects of temperature and pressure, because their thermodynamic models had excellent prediction performance, but sometimes these models could not give satisfactory prediction results.…”
Section: Introductionmentioning
confidence: 99%
“…When designing ILs for carbon capture using CAMD, 8 it is important to develop a reliable model for predicting the solubility of CO 2 in ILs. Many traditional thermodynamic or physical models, for example, PHSC state equation, Gibbs–Duhem function, cubic equation of state combined with UNIFAC, COSMO‐RS, and DFT could estimate gas solubility 9–16 . These models could well represent the effects of temperature and pressure, because their thermodynamic models had excellent prediction performance, but sometimes these models could not give satisfactory prediction results.…”
Section: Introductionmentioning
confidence: 99%
“…Due to the equivalent pressure is extremely high (up to several thousand bar), it is hard to determine the compressibility of ILs by using experimental measurements, and thus model prediction can be a viable option. A lot of theoretical models have been developed to predict the properties of ILs, which can be used as theoretical tools to screen ILs, such as Conductor-like Screening Model for Real Solvents (COSMO-RS), COSMO segment activity coefficient model (COSMO-SAC), Soave Redlich Kwong, Universal Quasi-Chemical Model, and so on (Maiti, 2009;Gonzalez-Miquel et al, 2011;Lee and Lin, 2015;Farahipour et al, 2016;Kamgar and Rahimpour, 2016;Theo et al, 2016). However, none of them can be used at high pressures.…”
Section: Introductionmentioning
confidence: 99%
“…In order to understand and predict the phase behavior of CO 2 and ionic liquid mixtures, Perturbed Hard Sphere Chain Equation of State (PHSC) has been selected to simulate the CO 2 absorption in a series of ionic liquids [7]. CO 2 solubility in ionic liquids had been calculated based on two thermodynamic models, namely the UNIQUAC model and the quantum model, based on COSMO-RS theory of interacting molecular surface charge [8]. Venkatramanet et al [9] used molecular descriptors based on quantum chemistry computations to predict the solubility of CO 2 in different ionic liquids.…”
Section: Introductionmentioning
confidence: 99%