作者: Muge Pilavtepe , Ozlem Yesil-Celiktas
DOI: 10.1016/J.SUPFLU.2013.07.020
关键词: Supercritical fluid extraction 、 Mass transfer 、 Desorption 、 Thermodynamics 、 Mass transfer coefficient 、 Chemistry 、 Supercritical fluid 、 Environmental pollution 、 Chromatography 、 Adsorption 、 Extraction (chemistry)
摘要: Abstract Posidonia oceanica residues were extracted with supercritical CO 2 in order to isolate phenolic compounds. The process was optimized by developing a mathematical model based on mass transfer mechanism consisting of adsorption fluid the solid particles, desorption solute and convective phase along column. Henry relation between concentrations surface ( Cs ) q approximated describe adsorption/desorption equilibrium. parameters such as solid-liquid film coefficient kf ), molecular diffusivity D AB axial dispersion ax estimated using empirical methods. linear driving force applied improve yield total acid recovery. optimum elicited 25 MPa, 323.15 K co-solvent ratio 20% yielding 34.97 μg per gram dry feed satisfactorily described extraction which can be used for scale-up purposes.