Yang, Chong, et al. The Journal of Chemical Thermodynamics 187 (2023): 107141.
1,3-Propanediol (1,3-PDO) has demonstrated superior performance as an extractant for the selective removal of phenol from coal tar systems containing toluene. Due to its strong hydrogen-bonding capability, 1,3-PDO forms stable associations with phenol, enabling its effective separation through liquid-liquid extraction (LLE).
In comparative ternary systems of phenol + toluene + solvent (either 1,2-PDO or 1,3-PDO), 1,3-PDO exhibited a significantly higher distribution of phenol into the extraction phase, confirming its greater affinity for phenol over toluene. Importantly, the mole fraction of 1,3-PDO in the raffinate phase was markedly lower than that of 1,2-PDO, indicating minimal solvent loss and enhanced solvent recovery during the process.
Furthermore, 1,3-PDO minimized the co-extraction of toluene into the extraction phase, reducing contamination and facilitating subsequent distillation steps. Ternary phase diagram analysis revealed that the system involving 1,3-PDO possesses a larger two-phase region than that with 1,2-PDO, indicating enhanced separation efficiency. The extraction performance of 1,3-PDO remained stable across a temperature range of 298.2-318.2 K, allowing the process to be effectively conducted under ambient conditions.
These findings establish 1,3-PDO as an optimal green solvent for phenol removal from aromatic mixtures, offering advantages in efficiency, selectivity, and process sustainability.