<> "The repository administrator has not yet configured an RDF license."^^ . <> . . . "Supercritical fluid extraction and solubilization of Carica papaya linn. leaves in ternary system with CO2 + ethanol solvents"^^ . "The supercritical fluid extraction of Carica papaya linn. leaves in the presence of CO2 solvent and ethanol modifier was carried out with respect to four operating parameters, namely temperature (40�60 °C), pressure (18�30 MPa), solvent flow rate (3�6 mL/min) and co-solvent ratio (3 � 5 vol), for the maximization of global extract yield of Carica papaya linn. leaves. The optimized parameters obtained are as follows: temperature of 57.47 °C, pressure of 26.62 MPa, solvent flow rate of 5.43 mL/min and co-solvent ratio of 4.98 with a predicted global extract yield of 0.0806 g. Five density-based solubility models, namely Chrastil, Bian et al., Bartle et al., Sparks et al. and Méndez-Santiago and Teja models were correlated against experimental solubility data. The Méndez-Santiago and Teja model were found to be more accurate with AARD of 1.36 and R2 value of 0.873 due to the non-linearity extraction profiles of papaya leaves. © 2020"^^ . "2020" . . "156" . . "Institution of Chemical Engineers"^^ . . . "Chemical Engineering Research and Design"^^ . . . "02638762" . . . . . . . . . . . . . . . . "B.L.F."^^ . "Chin"^^ . "B.L.F. Chin"^^ . . "S."^^ . "Yusup"^^ . "S. Yusup"^^ . . "Y.H."^^ . "Chai"^^ . "Y.H. Chai"^^ . . "M.S.H."^^ . "Ruslan"^^ . "M.S.H. Ruslan"^^ . . . . . "HTML Summary of #13298 \n\nSupercritical fluid extraction and solubilization of Carica papaya linn. leaves in ternary system with CO2 + ethanol solvents\n\n" . "text/html" . .