Article ID Journal Published Year Pages File Type
4768233 Fluid Phase Equilibria 2016 14 Pages PDF
Abstract
Vapor-liquid (VLE), liquid-liquid (LLE), and vapor-liquid-liquid equilibria (VLLE) data for the carbon dioxide + 1-dodecanol system at 293.15, 303.15, 313.15, 333.15, and 353.15 K up to 9.36 MPa and phase compositions of the two liquid phases and vapor phase as a function of temperature along the liquid-liquid-vapor (LLV) line are reported. Phase behavior measurements were made in a high-pressure visual cell with variable volume, based on the static-analytic method. The new experimental results are discussed and compared with available literature data. New measured and literature data for carbon dioxide + 1-dodecanol system were modeled with several cubic equations of state (EoS), namely the General Equation of State (GEOS), Peng-Robinson (PR), and Soave-Redlich-Kwong (SRK), using classical van der Waals (two-parameter conventional mixing rule, 2PCMR) mixing rules. A non-cubic hard-sphere perturbed equation of state, CSBM GEOS, was also considered, in order to test its capability to describe the equilibrium phase behavior in systems with molecular asymmetry.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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