نویسندگان | غلامحسین صدیفیان,حمید رضا باقری,محمدرضا برگستان,نداسادات سعادتی اردستانی |
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نشریه | Journal of the Taiwan Institute of Chemical Engineers |
شماره صفحات | 1 |
شماره مجلد | 161 |
ضریب تاثیر (IF) | ثبت نشده |
نوع مقاله | Full Paper |
تاریخ انتشار | 2024-08-15 |
رتبه نشریه | علمی - پژوهشی |
نوع نشریه | الکترونیکی |
کشور محل چاپ | ایران |
نمایه نشریه | JCR |
چکیده مقاله
Backgrounds To design the supercritical fluid processes for micro or nanosizing of solid solute components such as drugs, it is necessary to determine their solubility in solvents like supercritical carbon dioxide (SC-CO2). This important task is the first step for evaluating the process needed in supercritical fluid technology. Methods A statistical method was developed and used to determine the solubility of Gefitinib hydrochloride. The solubility measurements at various pressures and temperatures were conducted using UV-vis analysis. This research presents the equilibrium solubility of Gefitinib hydrochloride in SC-CO2 at temperatures and pressures ranging from 308 to 338 K and 120 to 270 bar, for the first time. Significant Findings The results indicated that the solubility of Gefitinib hydrochloride varied between (0.106-0.984) ×10-4. The Gefitinib hydrochloride mole fraction at constant temperature, increases with an increase in pressure. Meanwhile, a crossover point was observed. The solubility behavior was determined by the sPC-SAFT EoS and seven semi-empirical correlations. Both models have shown satisfactory agreements with the experimental data with AARD% of 9.86% and 7.46%. for the sPC-SAFT EoS and the Chrastil, respectively. Finally, the total, solvation, and vaporization enthalpies of the drug/SC-CO2 binary system were determined using semi-empirical correlations, for the first time.
tags: Gefitinib hydrochloride; Semi-empirical models; Solubility; sPC-SAFT; Supercritical CO2