The supercritical fluid extraction of orange essential oil was studied
using dehydrated orange peel (0.0538 kg H2O kg(-1) dm) from naveline
cultivars as raw material and CO2 as solvent. The effect of operation
conditions was analyzed in a series of experiments at 313 and 323 K an
d pressures between 1 and 25 MPa. Furthermore, the effect of CO2 flow
rate and particle size of orange peel was studied in the range of 0.5
to 3.5 kg h(-1) and 0.1 to 10 mm. The subcritical CO2 dissolves hardly
any essential oils, however, on reaching the critical point, the amou
nt of essential oils dissolved increased with pressure, within the ran
ge of pressures considered in this study. Increasing solvent mass flow
decreased the extraction efficiency while increasing particle size of
orange peel decreased the extraction rate. For a rapid extraction, pa
rticle sizes lower than 2 mm and solvent mass flows lower than 2.5 kg
h(-1) are adequate. A model based on the assumption of plug flow of a
supercritical solvent through a fixed bed of milled material was appli
ed to analyze the experimental. results. The model successfully fitted
the experimental data. The collected extracts were orange in color du
e to the carotenoid and flavonoid content. During the process, water w
as extracted in the final stage of the extraction.