Experimental Vapor–Liquid Equilibria and Thermodynamic Modeling of the Methanol + n-Heptane and 1-Butanol + Aniline Binary Systems
Author:
Affiliation:
1. Natural Gas Engineering Department, School of Chemical and Petroleum Engineering, Shiraz University, Mollasadra Avenue, Shiraz 71348-51154, Iran
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/acs.jced.7b00766
Reference32 articles.
1. A systematic study of methanol+n-alkane vapor–liquid and liquid–liquid equilibria using the CK-SAFT and PC-SAFT equations of state
2. Vapor−Liquid Equilibrium of Binary Mixtures. 1. Ethanol + 1-Butanol, Ethanol + Octane, 1-Butanol + Octane
3. Modelling LLE and VLE of methanol+n-alkane series using GC-PC-SAFT with a group contribution kij
4. Vapor-Liquid Equilibria of Methanol + Hexane, Methanol + Heptane, Ethanol + Hexane, Ethanol + Heptane, and Ethanol + Octane at 298.15 K
5. Thermodynamic excess properties and vapor–liquid equilibria of binary and ternary mixtures containing methanol, tert-amyl methyl ether and an alkane
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2. Modelling low pressure LLE and VLE of methanol/alkane mixtures with a modified Peng-Robinson EoS and the Huron-Vidal mixing rules;Fluid Phase Equilibria;2021-10
3. MEASUREMENTS AND THERMODYNAMIC MODELING OF VAPOR-LIQUID EQUILIBRIA FOR BINARY SYSTEMS OF ISOPROPYL CHLOROACETATE WITH CYCLOHEXANE, ISOPROPANOL AND BENZENE AT 101.3 kPa;Brazilian Journal of Chemical Engineering;2019-12
4. Application of the molecular interaction volume model (MIVM) and its modified form to organic vapor-liquid equilibria;Fluid Phase Equilibria;2019-04
5. Measurements and Prediction of Melting Temperature and Eutectic Point of Binary Fatty Acids Based on Wilson Activity Model;PHYS CHEM RES;2019
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