1964
DOI: 10.1021/je60021a018
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Vapor-Liquid Equilibria for the Methanol-Toluene System.

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1967
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Cited by 24 publications
(12 citation statements)
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“…Figure 5 shows the dependence of methanol concentration in the permeate on methanol concentration in the feed for the pervaporation of a methanol–toluene mixture at 20 °C using three types of films. To compare results of the pervaporation tests, Figure 5 shows also a vapor–liquid equilibrium curve for the methanol–toluene system at 760 mm Hg [ 51 ]. The run of the vapor–liquid equilibrium curve differs essentially from the permeate–feed concentration curves in the pervaporation of the methanol–toluene mixture.…”
Section: Resultsmentioning
confidence: 99%
“…Figure 5 shows the dependence of methanol concentration in the permeate on methanol concentration in the feed for the pervaporation of a methanol–toluene mixture at 20 °C using three types of films. To compare results of the pervaporation tests, Figure 5 shows also a vapor–liquid equilibrium curve for the methanol–toluene system at 760 mm Hg [ 51 ]. The run of the vapor–liquid equilibrium curve differs essentially from the permeate–feed concentration curves in the pervaporation of the methanol–toluene mixture.…”
Section: Resultsmentioning
confidence: 99%
“…The com bustion characteristics of the m ethan o l/to lu en e m ixtures can be partially understood in light of th e fractional vaporization of the tw o fuel com ponents. A t atm ospheric pressure, m eth an o l/to lu en e v ap o u r-liq u id equilibrium d a ta exhibit a negative azeotrope a t a m ethanol mole fraction of 0.89 (Burke et al 1964), which corresponds to the 25% by volume toluene m ixture. Because of the neg ativ ity of th e azeotrope, the heating of any non-azeotropic m ixture during com bustion will ten d to push the droplet com position fu rth er aw ay from the azeotrope.…”
Section: Discussionmentioning
confidence: 99%
“…Alcohol-aromatic mixtures such as a toluene-methanol system are commonly used in the petrochemical and pharmaceutical industries. This system forms an azeotropic with 32 wt% toluene at a constant pressure of 101.3 kPa [27]. Over the past two decades, the separation of such a mixture has attracted the particular attention of researchers in different fields due to the importance of the components in the chemical and pharmaceutical industries [28][29][30][31][32][33][34][35][36][37][38][39].…”
Section: Introductionmentioning
confidence: 99%