Some information on calculating the liquid-liquid equilibrium of ternary systems. an improvement of prediction of liquid-liquid equilibrium in ternary systems from binary equilibrium data
1982 ◽
Vol 47
(5)
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pp. 1420-1432
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Keyword(s):
A possibility is described of improving the prediction of ternary liquid-liquid equilibrium data from binary ones by using three-parameter equations for calculating activity coefficients. The parameters for completely miscible pairs of liquids were determined from their vapour-liquid equilibrium data and those for partially miscible pairs of liquids from their mutual solubilities and from one limiting activity coefficient. A quantitatively correct prediction of the liquid-liquid equilibrium data was achieved in all cases by means of three different equations (NRTL equation, Redlich-Kister equation and Wilson equation modified by Novák and coworkers) in four hydrocarbon-hydrocarbon-polar solvent systems investigated.
2009 ◽
Vol 278
(1-2)
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pp. 9-14
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Keyword(s):
1973 ◽
Vol 28
(5)
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pp. 1213-1221
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2008 ◽
Vol 73
(1)
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pp. 73-85
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1982 ◽
Vol 86
(8)
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pp. 761-761
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Keyword(s):
2019 ◽
Vol 128
◽
pp. 215-224
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1977 ◽
Vol 10
(5)
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pp. 400-402
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1999 ◽
Vol 16
(1)
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pp. 7-17
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