Isobaric Vapor−Liquid Equilibria for Binary and Ternary Systems Composed of 2-Methoxy-2-methylpropane, Ethanol, 2-Methyl-2-propanol, and Octane at 101.3 kPa
Author:
Affiliation:
1. Department of Industrial Chemistry, College of Industrial Technology, Nihon University, 1-2-1, Izumi-cho, Narashino, Chiba 275-8575, Japan
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/je990287j
Reference14 articles.
1. Isobaric Vapor−Liquid Equilibria for 2-Methoxy-2-methylpropane + Ethanol + Octane and Constituent Binary Systems at 101.3 kPa
2. Vapor–liquid equilibria for binary and ternary systems composed of 2-methoxy-2-methyl propane, 2-methyl-2-propanol, and octane at 101.3 kPa
3. Vapor-liquid equilibria of 2,3-dimethylbutane + methanol or ethanol at 101.3 kPa
4. Liquid-vapour equilibrium. XLII. Systems: ethyl alcohol-water-tert-butyl alcohol and ethyl alcohol-water-isobutyl alcohol
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2. Isobaric Binary and Ternary Vapor–Liquid Equilibrium for the Mixture of n-Hexane, Methylcyclopentane and N-Methylpyrrolidone;Journal of Solution Chemistry;2021-09-23
3. Development of the NRTL functional activity coefficient (NRTL-FAC) model using high quality and critically evaluated phase equilibria data. 1;Fluid Phase Equilibria;2021-08
4. Thermal Diffusivity of 2-Methoxy-2-methylpropane at Temperatures from (303.15 to 493.15) K and Pressures from (1.5 to 10) MPa;Journal of Chemical & Engineering Data;2014-11-04
5. Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa;Journal of Chemical & Engineering Data;2003-11-26
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