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Experimental Solubility Measurements of Fenoprofen in Supercritical Carbon Dioxide

Samyar ZabihiSamyar Zabihi, Shazand-Arak Oil Refinery Company, Department of Process Engineering, Research and Development Department, Arak 381314-3553 IranYaghoub RahnamaSchool of Chemical and Petroleum Engineering, Shiraz University, Shiraz 71345-1719, IranAmir SharafiSamyar Zabihi, Shazand-Arak Oil Refinery Company, Department of Process Engineering, Research and Development Department, Arak 381314-3553 IranFatemeh BorousanDepartment of Chemistry, Yasouj University, Yasouj 75914-353, IranAli Zeinolabedini HezaveIncubation Centre of Science and Technology Park, Fanavari Arena Exir Sabz Company, Arak 381314-3553, IranSaeed ShirazianDepartment of Chemical Sciences, Bernal Institute, University of Limerick, Limerick V94 T9PX, Ireland
2020en
ABI

Аннотация

In the current investigation, the solubility of fenoprofen as a nonsteroidal anti-inflammatory drug in supercritical CO2 (SC-CO2) is measured by employing a motorized PVT (pressure–volume–temperature) equilibrium cell. The solubility measurements were carried out in temperatures between 308 and 338 K and pressures between 12 and 40 MPa. The measured data reveals that the solubility of fenoprofen (mole fraction) lies between 2.01 × 10–5 and 4.20 × 10–3, depending on the thermodynamic conditions. Besides the experimental measurement of fenoprofen solubility, thermodynamic modeling of solubility using five different density-based semi-empirical correlations was carried out. The models were considered with only three fitting parameters, namely, Mendez-Santiago and Teja (MST), Bartle et al., Kumar and Johnston (K–J), Chrastil, and Garlapati and Madras models. The results revealed that among the examined models, the Bartle et al. model was the most accurate one with the lowest average absolute relative deviation percent (AARD %) of 6.58% for the studied drug, while the K–J model leads to poor prediction with an AARD % of 9.60%.

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