Post-processing of a lavender flowers solvent extract using supercritical CO2 fractionation

被引:10
|
作者
Zanotti, Alessandra [1 ]
Baldino, Lucia [1 ]
Scognamiglio, Mariarosa [1 ]
Reverchon, Ernesto [1 ]
机构
[1] Univ Salerno, Dept Ind Engn, Via Giovanni Paolo II 132, I-84084 Fisciano, SA, Italy
关键词
Lavender concrete; Lavender essential oil; Supercritical fluid extraction; Supercritical fractionation; Mathematical modelling; ESSENTIAL OIL; FLUID EXTRACTION; CONCRETE FRACTIONATION; SC-CO2; EXTRACTION; GROWTH-FUNCTION; MODEL; CULTIVARS; YIELD;
D O I
10.1016/j.jtice.2023.104901
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Background: Supercritical Fluid Extraction (SFE) was performed using an unconventional material, the solid extract of lavender flowers obtained by liquid solvent extraction and subsequent solvent elimination.Methods: Systematic extraction experiments were carried out at 8 MPa and 40 degrees C, and the extract was frac-tionated in semi-continuous mode in the SFE plant. To understand mass transfer phenomena driving the process, CO2 mass flow rates ranging between 0.60 and 1.50 kg/h were used, and yield vs. time curves were obtained. Significant findings: Fractionation produced a cuticular waxes selective precipitation in the first separator and the floral fragrance in the second separator. The most abundant species in the extract were tau-cadinol (13%), lav-andulol (10.5%), beta-caryophyllene (10%), viridiflorene (8.5%), isocaryophyllene (6%), cedrenalol (4.5%), linalool (4%) and 1,8-cineol (4%). The fragrance contained no waxes, indicating that the fractionation was successful. At higher mass flow rates (from 0.90 to 1.50 kg/h), an asymptotic extraction yield of 5.2% w/w was obtained; whereas, at lower mass flow rates, the extraction yield was lower (2.3% w/w) since the vegetable bed was not completely wetted by the extraction fluid. The overall results indicated that an external mass transfer resistance controlled the process.
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页数:6
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