2020
DOI: 10.1021/acssuschemeng.9b07358
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Screening of Imidazole Ionic Liquids for Separating the Acetone–n-Hexane Azeotrope by COSMO-SAC Simulations and Experimental Verification

Abstract: Ionic liquids have received wide attention as green recyclable extractants. In view of their broad applicability, in the current work, ionic liquids were explored for their ability to extract acetone from n-hexane. Based on the conductor-like screening model for the segment activity coefficient, the surface charge densities of 15 kinds of cations, 19 kinds of anions, acetone, and n-hexane were calculated via quantum chemistry approaches. The infinite dilution activity coefficients of the ionic liquid–acetone–n… Show more

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Cited by 43 publications
(21 citation statements)
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“…The BTX absorption processes' (TEG and [EMIM][Tf 2 N]) conceptual designs were conducted via ASPEN PLUS software. Moreover, the UNIFAC-Lei model 22 was employed to evaluate the thermodynamic properties and phase equilibrium-related parameters. The equilibrium (EQ) stage model was also used for desorption column simulation.…”
Section: ■ Methodologymentioning
confidence: 99%
“…The BTX absorption processes' (TEG and [EMIM][Tf 2 N]) conceptual designs were conducted via ASPEN PLUS software. Moreover, the UNIFAC-Lei model 22 was employed to evaluate the thermodynamic properties and phase equilibrium-related parameters. The equilibrium (EQ) stage model was also used for desorption column simulation.…”
Section: ■ Methodologymentioning
confidence: 99%
“…The map is divided into three zones by two black vertical solid lines (⊞ = ±0.0084 e Å −2 ), which are the left-hand hydrogen bond donor zone, the middle non-polar zone and the righthand hydrogen bond receptor zone. 55 , 56 When the peak value of one substance is farther away from the dimension of 0.0084 e Å −2 , it means that it has a stronger hydrogen bond donor or acceptor capability. From Fig.…”
Section: ⊞-Profilesmentioning
confidence: 99%
“…As such, pragmatic and robust computational tools provide a possible remedy to overcome this hurdle, with the capability of rapidly determining potential HFCs replacements, satisfying environmental and technical requirements. With the rise of thermodynamic modeling approaches and computational power, such paradigms have been successfully developed for varying applications such as screening of materials for CO 2 capture and solvents for other separation processes. The success of these paradigms is entirely dependent on the accuracy and robustness of the chosen thermodynamic model . In this regard, molecular-based equations of state (EoSs) such as those routed on the statistical associating fluid theory (SAFT) have become indispensable tools in modeling the thermodynamic behavior of complex fluids.…”
Section: Introductionmentioning
confidence: 99%