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Liquid-liquid equilibria of fuel oxygenate + water + hydrocarbon mixtures. 2

Journal Article · · Journal of Chemical and Engineering Data; (United States)
DOI:https://doi.org/10.1021/je00017a070· OSTI ID:6548502
 [1];  [2]
  1. Technische Univ. Berlin (Germany). Inst. fuer Thermodynamik und Reaktiontechnik
  2. Univ. of Delaware, Newark, DE (United States)
The liquid-liquid equilibria of water + n-decane, water + n-hexadecane, and water + methylcyclohexane have been measured separately with the two oxygenates 2-methoxy-2-methylbutane (tertiary amyl methyl ether or TAME) and 2-methyl-2-butanol (tertiary amyl alcohol or TAOH) at 25 C. All of these systems exhibit type 2 liquid-liquid phase diagrams, through the shapes of the diagrams for the TAME and TAOH systems are quite different because of the much higher solubility of water in TAOH than TAME. One of the observations from their experimental data is that the addition of either TAME or TAOH to a hydrocarbon + water mixture results in an increased water solubility in the hydrocarbon phase and a decreased hydrocarbon solubility in the aqueous phase. This observation may be important when both the water pollution potential of possible gasoline reformulations and the sensitivity of the gasoline to water are assessed. The authors have found that the general features of the liquid-liquid phase diagrams can be accurately correlated with either the NRTL or UNIQUAC model, through some of the high dilution concentrations are incorrectly described. Finally, the liquid-liquid UNIFAC model leads to qualitatively correct predictions for the liquid-liquid equilibria of the systems studied.
OSTI ID:
6548502
Journal Information:
Journal of Chemical and Engineering Data; (United States), Journal Name: Journal of Chemical and Engineering Data; (United States) Vol. 40:1; ISSN JCEAAX; ISSN 0021-9568
Country of Publication:
United States
Language:
English