From
palm oil valuable compounds like the tocochromanols, carotenoids, phytosterols, and others can be derived. Enrichment to highly concentrated fractions is hindered by the enormous number of components involved, the very low volatility, the very low
solubility of many of the compounds in organic solvents, and the high
viscosity of the mixtures to be processed. Starting materials for the new process are enriched fractions of tocochromanols (about 20 to about 50 wt.-%) and / or carotenoids (about 10 to 30 wt.-%) from
palm oil obtained by conventional processes, or by
counter current multistage processes with
supercritical carbon dioxide. These processes, not addressed here, may comprise: Removal of free fatty acids,
transesterification of the triglycerides to methyl or ethyl esters, removal of the esters, e.g. by
short path distillation, separation of the tocochromanol fraction from the
carotenoid fraction by cooling. In the new process, fractions derived from crude
palm oil, already enriched to some extent in tocochromanols, carotenoids, phytosterols, and others, are being treated by
supercritical fluid technology in a unique combination of
counter current separation with
selective adsorption and
desorption using supercritical fluids. A first enrichment, comprising one or more separation steps by application of a
near critical or a
supercritical fluid in a single or multistage (
counter current)
separation process is combined appropriately with a second enrichment step wherein the product of the first enrichment step is directly adsorbed on an adsorbent (silicagel) by passing the product flow over a
fixed bed of adsorbent without substantial pressure change, and subsequent
desorption with the same (or an other)
near critical or
supercritical fluid at the same or a different pressure as in the first separation, or by a pre-designed sequence of pressures and temperatures. For the tocochromanol enrichment,
carbon dioxide at
near critical conditions above the critical temperature of
carbon dioxide is used. For the
carotenoid enrichment,
propane at near critical conditions below the critical temperature of
propane is used.