Isothermal Vapor–Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
Author:
Affiliation:
1. Thermodynamics Research Unit, School of Engineering, University of KwaZulu-Natal, Durban, 4041, South Africa
2. MINES-ParisTech, CEP/TEP−Centre Energétique et Procédés, 35 rue Saint Honoré, 77305 Fontainebleau, France
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/je201032t
Reference20 articles.
1. Liquid–Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
2. Phase equilibrium properties of binary systems with diacetyl from a computer controlled vapour–liquid equilibrium still
3. Isobaric Vapor−Liquid Equilibria for the Systems Propionic Acid + Butyric Acid, Isobutyric Acid + Butyric Acid, Butyric Acid + Isovaleric Acid, and Butyric Acid + Hexanoic Acid at 14 kPa
4. Monoethanolamine as an Extractive Solvent for the n-Hexane + Benzene, Cyclohexane + Ethanol, and Acetone + Methanol Binary Systems
5. Vapor−Liquid Equilibrium Measurements of MTBE and TAME with Toluene
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1. Vapor–Liquid Equilibrium (P–T–x–y) Measurements and Modeling of propan-1-ol/propan-2-ol + oct-1-ene in the Range of T = (313.2–353.2) K;Journal of Chemical & Engineering Data;2022-09-13
2. Comparison of SAFT-VR-Mie and CP-PC-SAFT in predicting phase behavior of associating systems III. Aliphatic hydrocarbons - 1-propanol, 1-butanol and 1-pentanol;Journal of Molecular Liquids;2019-04
3. Isobaric Vapor–Liquid Equilibrium for Binary Systems of Thioglycolic Acid with Water, Butyl Acetate, Butyl Formate, and Isobutyl Acetate at 101.3 kPa;Journal of Chemical & Engineering Data;2016-12-20
4. PVT properties of 1-propanol in the critical and supercritical regions;The Journal of Supercritical Fluids;2016-11
5. Vapor–Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa;Journal of Chemical & Engineering Data;2014-04-07
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