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Publikováno v:
Fluid Phase Equilibria. 61:89-98
Equilibrium tie line data have been determined at 60 and 100°C with sulfolane and five model hydrocarbon mixtures consisting of butylbenzene—dodecane, hexylbenzene—dodecane, hexylbenzene—cetane, octylbenzene—dodecane and octylbenzene—cetan