1. Phase Equilibriaof the Carbon Dioxide 1-DecanolSystem at High Pressures.
- Author
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IoniţaÌ, Simona, Feroiu, Viorel, and GeanaÌ, Dan
- Subjects
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PHASE equilibrium , *DECANOL , *HIGH pressure (Technology) , *VAPOR-liquid equilibrium , *TEMPERATURE effect , *CRITICAL point (Thermodynamics) - Abstract
Inthis work experimental vaporâliquid equilibrium (VLE)data and three-phase vaporâliquidâliquid equilibrium(VLLE) data are presented for the carbon dioxide 1-decanol system.The VLE data were measured at five temperatures, (303.2, 308.2, 323.2,333.2, and 343.2) K, and pressures up to 16 MPa. The VLLE data coverpressureâtemperature (PâT) values from289 K and 5 MPa to the upper critical end point (UCEP). We have usedtwo models to represent the complex fluid phase behavior (PâTcritical curve, VLLE line, and VLE isotherms)of the carbon dioxide 1-decanol system: the cubic general equationof state (GEOS) and PengâRobinson (PR) equation in conjunctionwith van der Waals two parameters conventional mixing rules (2PCMR).A correlation method involving temperature-dependent interaction parametersand a semipredictive approach with independent temperature interactionparameters have been used. Comparisons with experimental data reportedin this work and available in the literature indicate that the topologyof fluid phase behavior is satisfactorily given by the semipredictiveprocedure both for the critical line and in subcritical region, consideringthe relative simple used cubic equations of state. [ABSTRACT FROM AUTHOR]
- Published
- 2013
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