2002
DOI: 10.1021/je010272x
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Vapor−Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System

Abstract: Vapor-liquid equilibrium data were presented for the ethanol + 2-methyl-1-butanol system, obtained at three operating pressures. A modified Othmer still was used for data acquisition. When the Herington area test was applied to the experimental result, good thermodynamic consistency was found. Several equations based on both classic G E models (Margules and Van Laar) and local composition based models (Wilson, NRTL, and UNIQUAC) were used for data correlation. The UNIFAC group contribution model was applied to… Show more

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Cited by 9 publications
(11 citation statements)
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“…The experimental data are listed in Table 2, where T is the temperature, p is the vapor pressure and w is the mass fraction. Table 3 gives boiling temperatures and Antoine equation constants (compared with literature data) of ethanol [17].…”
Section: Vapor Pressures Of the Pseudo-binary Mixturesmentioning
confidence: 99%
“…The experimental data are listed in Table 2, where T is the temperature, p is the vapor pressure and w is the mass fraction. Table 3 gives boiling temperatures and Antoine equation constants (compared with literature data) of ethanol [17].…”
Section: Vapor Pressures Of the Pseudo-binary Mixturesmentioning
confidence: 99%
“…For this study, the experimental VLE data on the three binary systems that compose the ternary system are needed, and these data have been taken from the literature. [9][10][11] NRTL Electrolyte Model. When the NRTL electrolyte model is used with systems constituted by two solvents plus a salt, the equilibrium condition refers only to the solvents since they are the only species present in both phases.…”
Section: Resultsmentioning
confidence: 99%
“…The experimental vapor pressure data of ethanol are compared with the literature data in Fig. 2 [22], and Table 5 gives boiling temperatures and Antoine equation constants (compared with literature data) of ethanol and methylcyclohexane [22][23][24].…”
Section: Vapor Pressures Of the Pseudo Binary Mixturesmentioning
confidence: 99%