Journal of Chemical & Engineering Data · 2004 · 188 citations · 26 references
Natural SciencesChemical EngineeringChemistryCondensed Matter PhysicsInorganic ChemistryPhase TransformationsHigh-pressure ThermodynamicsPhase DiagramsPhase EquilibriaPhase RelationsPhase TransitionsThermodynamics Of Phase EquilibriaBubble Point PressureCarbon DioxideHigh-pressure Phase BehaviorHigh-pressure Phase DiagramsHigh-pressure Phase RelationsIonic LiquidsPhase Behavior Of Carbon DioxidePhase Equilibria At High Pressure
The phase behavior of the binary system consisting of the supercritical fluid carbon dioxide (CO 2 ) and the ionic liquid 1-butyl-3-methylimidazolium tetrafluoroborate ([bmim][BF 4 ]) was studied experimentally. A synthetic method was used to measure its phase behavior. Bubble-point pressures of the system CO 2 + [bmim][BF 4 ] are reported for carbon dioxide concentrations ranging from (10.22 to 60.17) mole % and within a temperature range of (278.47 to 368.22) K. The CO 2 + [bmim][BF 4 ] binary system has a two-phase liquid−vapor region extending up to very high pressures. Most likely, the type of fluid-phase behavior is type III according to the classification of Scott and Van Konynenburg. The experimental results obtained were compared with the available phase behavior data of the binary system CO 2 + 1-hexyl-3-methylimidazolium tetrafluoroborate ([hmim][BF 4 ]) to investigate the effect of the length of the alkyl group on the phase behavior of this type of system. A larger alkyl group leads to lower bubble-point pressures and, therefore, to higher solubilities of carbon dioxide in the imidazolium-based ionic liquid.
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