High-pressure phase equilibria of carbon dioxide + 1,4-dioxane binary system
نویسندگان
چکیده
New isothermal vapor–liquid equilibrium (VLE) data for the carbon dioxide + 1,4-dioxane system are reported at four temperatures (323.15, 333.15, 343.15, and 353.15) K pressures up to 122.7 bar. The critical curve was also measured 158.8 bar 420.15 K. Phase behavior measurements were performed in a high-pressure windowed cell with variable volume, using static-analytical method phases sampling by rapid online sample injectors (ROLSI) coupled gas chromatograph (GC) analysis. experimental results of this study compared scarce available literature data. new all binary modelled cubic Soave–Redlich–Kwong (SRK) Peng–Robinson (PR) equations state (EoS) classical van der Waals mixing rules (two-parameter conventional rules, 2PCMR). modeling showed that SRK PR models can accurately predict phase studied.
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ژورنال
عنوان ژورنال: Fluid Phase Equilibria
سال: 2021
ISSN: ['0378-3812', '1879-0224']
DOI: https://doi.org/10.1016/j.fluid.2021.113181