Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4-trimethylpentane and 1-hexene at 313.15K
Author:
Publisher
Elsevier BV
Subject
Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering
Reference31 articles.
1. Excess thermodynamic functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and GE for methyl tert-butyl etherbenzenecyclohexane at 313.15 K
2. Vapor–Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
3. Vapor–Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
4. Vapour–liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T=313.15K
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
Cited by 3 articles. 订阅此论文施引文献 订阅此论文施引文献,注册后可以免费订阅5篇论文的施引文献,订阅后可以查看论文全部施引文献
1. Thermodynamic properties for 1-hexene – Measurements and Modeling;The Journal of Chemical Thermodynamics;2023-01
2. P-x isothermal equilibrium data for two ternary systems containing long-chain bioalcohols: (1-butanol or 2-butanol + cyclohexane + methylbenzene) at 313.15 K;The Journal of Chemical Thermodynamics;2020-02
3. Isothermal vapor–liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol+1-hexene+methylbenzene at 313.15K;Fluid Phase Equilibria;2015-01
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