High-Pressure Bubble-and Dew-Point Data for SystemsContaining CO<sub>2</sub> + (C<sub>8</sub>/C<sub>10</sub> 1‑Alcoholwith C<sub>12</sub>/C<sub>14</sub>/C<sub>16</sub> Methyl Ester) Systems
Six new high-pressure bubble- and dew-point data sets have been generated for ternary systems containing carbon dioxide (C<sub>8</sub> or C<sub>10</sub> 1-alcohols) and (C<sub>12</sub> or C<sub>14</sub> or C<sub>16</sub> methyl esters). These data were measured at a fixed reduced solute mass fraction of 0.5000 between a total solute mass fraction of 0.020 to 0.640 at temperatures between 308.15 and 358.15 K. The CO<sub>2</sub> + 1-octanol + methyl tetradecanoate/methyl hexadecanoate and CO<sub>2</sub> + 1-decanol + methyl hexadecanoate systems were shown to be cosolvent due to preferential interactions between like molecules. In comparison to the CO<sub>2</sub> + 1-alcohol + <i>n</i>-alkane ternary systems, the CO<sub>2</sub> + 1-alcohol + methyl ester ternary systems are consistently less cosolvent, indicating that cross-association potentially occurs between the 1-alcohol and methyl ester molecules, decreasing the solubility enhancement that is expected due to the disruption of the hydrogen bonding between neighboring 1-alcohols by the methyl ester. The RK-Aspen model is shown to provide an adequate description of the measured phase behavior data including only solute + solvent binary interaction parameters.
Publication Details
- Journal
- Figshare
- Published
- 2025-02-12
- DOI
- https://doi.org/10.1021/acs.jced.4c00702.s001
- Primary Topic
- 3D Surveying and Cultural Heritage
- Type
- article
- Field-Weighted Citation Impact
- 0.00