1995
DOI: 10.1016/0378-3812(95)02756-5
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Vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons at 298.15 K and 313.15 K

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Cited by 59 publications
(36 citation statements)
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“…The purity of the products after degassing was checked by gas chromatography, and the values were > 99.8 % (GC) for all the compounds. , and whose performance has been described detailed in previous papers 10,11 .…”
Section: Methodsmentioning
confidence: 99%
“…The purity of the products after degassing was checked by gas chromatography, and the values were > 99.8 % (GC) for all the compounds. , and whose performance has been described detailed in previous papers 10,11 .…”
Section: Methodsmentioning
confidence: 99%
“…(12)(13)(14) The data reduction of the binary and ternary mixtures has been performed using Barker's method (15) according to well-established procedures. (16,17) A developed computer program described elsewhere (1) has been used to implement the technique.…”
Section: Results and Correlationsmentioning
confidence: 99%
“…The experimental data for {x 1 (27) and the excess molar entropy S E m is calculated from the thermodynamic relation (28)(29)(30) We have not been able to make measurements in this region of the (vapour + liquid + liquid) equilibrium because the technique is not adequate for very low mole fractions. The pressure surface, figure 4, shows a maximum at 66.238 kPa which corresponds to the azeotrope {x 1 CH 3 OC(CH 3 ) 2 CH 3 + (1 − x 1 )CH 3 OH}, and a minimum at 12.331 kPa corresponding to the pressure of pure n-heptane.…”
Section: Discussionmentioning
confidence: 99%
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