Journal of Molecular Liquids, Journal Year: 2024, Volume and Issue: unknown, P. 126343 - 126343
Published: Oct. 1, 2024
Language: Английский
Journal of Molecular Liquids, Journal Year: 2024, Volume and Issue: unknown, P. 126343 - 126343
Published: Oct. 1, 2024
Language: Английский
Journal of Molecular Liquids, Journal Year: 2025, Volume and Issue: unknown, P. 127026 - 127026
Published: Jan. 1, 2025
Language: Английский
Citations
0Journal of Chemical & Engineering Data, Journal Year: 2025, Volume and Issue: unknown
Published: Jan. 29, 2025
Language: Английский
Citations
0AIChE Journal, Journal Year: 2025, Volume and Issue: unknown
Published: March 4, 2025
Abstract The separation of azeotropes is great significance for improving product quality, optimizing production processes, and promoting the development related technologies. This study used quaternary ammonium salt‐based deep eutectic solvents (DESs) to separate azeotropic ethanol methyl acetate mixtures. COSMO‐RS software was facilitate screening extractants. best extractant selected from 16 hydrogen bond acceptors 38 donors, vapor–liquid equilibrium experiments were subsequently conducted experimental verification. experiment demonstrated that DESs synthesized alcohol salt chemicals relatively practical, with effect varying according diols employed as donors. Concurrently, quantitative calculations conduct a microscopic analysis elucidate underlying mechanism spatial hindrance on performance ethanol–methyl acetate.
Language: Английский
Citations
0Separation and Purification Technology, Journal Year: 2024, Volume and Issue: 359, P. 130587 - 130587
Published: Nov. 17, 2024
Language: Английский
Citations
3The Canadian Journal of Chemical Engineering, Journal Year: 2024, Volume and Issue: unknown
Published: Nov. 10, 2024
Abstract Instead of the classical molecular simulation widely implemented for estimating vapour–liquid equilibrium (VLE), a quantum chemical (QC) dynamics was applied to VLE estimation in three typical systems that include deep eutectic solvent (DES) and an ionic liquid (IL). In addition, radial distribution function (RDF) derived from QC examine behaviour phase. A mean absolute error 2.72% obtained compared experimental data. The RDF analysis explains relative volatility increase acetic acid water binary system with propyl acetate solvent. This indicated DES mixture comprising glycerol choline chloride facilitated separation i ‐propanol. interaction between ethyl sulphate pair help 1‐ethyl‐3‐methylimidazolium as IL is stronger than ethanol water, which how improves vapour
Language: Английский
Citations
1Published: Jan. 1, 2024
Language: Английский
Citations
0Published: Jan. 1, 2024
Language: Английский
Citations
0Chemical Engineering Journal, Journal Year: 2024, Volume and Issue: 499, P. 156576 - 156576
Published: Oct. 11, 2024
Language: Английский
Citations
0Journal of Molecular Liquids, Journal Year: 2024, Volume and Issue: unknown, P. 126343 - 126343
Published: Oct. 1, 2024
Language: Английский
Citations
0