Vapor–Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K-Reference-Cited by-同舟云学术

Vapor–Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K

Published:2012-02-24 Issue:3 Volume:57 Page:982-987
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Belabbaci Aouicha¹,Villamañán Rosa M.²,Negadi Latifa¹,Martín M. Carmen²

Affiliation:

1. LATA2M, Laboratoire de Thermodynamique et Modélisation Moléculaire, University AbouBekr Belkaid of Tlemcen, P.O. Box 119, Tlemcen 13000, Algeria

2. Grupo de Termodinámica y Calibración (TERMOCAL), Departamento Ingeniería Energética y Fluido Mecánica, ETS de Ingenieros Industriales, Universidad de Valladolid, E-47071 Valladolid, Spain

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/je201284y

Reference32 articles.

1. Vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons at 298.15 K and 313.15 K

2. Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and GE for methyl tert-butyl etherbenzenecyclohexane at 313.15 K

3. Thermodynamics of Octane-Enhancing Additives in Gasolines: Vapor−Liquid Equilibrium of the Ternary Mixtures Methyl tert-Butyl Ether + Heptane + Benzene and Methyl tert-Butyl Ether + Benzene + 1-Hexene at 313.15 K

4. Vapor−Liquid Equilibrium of Binary and Ternary Mixtures Containing Isopropyl Ether, 2-Butanol, and Benzene at T = 313.15 K

5. Characterization and modelling of a gasoline containing 1,1-dimethylethyl methyl ether (MTBE), diisopropyl ether (DIPE) or 1,1-dimethylpropyl methyl ether (TAME) as fuel oxygenate based on new isothermal binary vapour–liquid data

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