Adsorption equilibria of fatty acids between methanol/water and reversed-phase chromatographic adsorbents

The adsorption equilibria are discussed for fatty acids 16:1n-7, 16:2n-4, and 20:5n-3 (eicosapentaenoic acid, EPA). These fatty acids are major components of a polyunsaturated fatty acid concentrate from the microalga Phaeodactylum tricornutum. The solvents used were methanol/water (1% acetic acid) mixtures of different compositions, and the adsorbents used were chromatographic reversed-phases octylsilyl C-8 octadecylsilyl C-18, and dodecylsilyl C-22 of different particle and pore sizes. The kinetic studies showed that equilibrium was attained instantaneously, suggesting an absence of mass transfer limitations. The equilibrium data were fitted by the Freundlich isotherm. The separation efficiency of EPA from 16:1 n-7 and 16:2n-4 in all the adsorbent-solvent systems was compared in terms of the separation factors alpha (EPA/16:2n-4) K-EPA/K16:2n-4 and alpha (16:1n-7/EPA) = K16:1n-7/K-EPA' where K; is the fatty acid distribution ratio between the stationary and the liquid phases. The EPA separation from 16:1n-7 and 1 6:2n-4 by liquid chromatography could be predicted using the Craig model for the various solvent-adsorbent combinations. The best adsorbents for purifying EPA were: C-18, PEP, 8 mum, 100 Angstrom, and C-22, 10 mum, 100 Angstrom, and the best solvent was methanol/water (1% acetic acid) 75:25, w/w.