Abstract:The supercritical fluid extraction of corn germ oil has been studied in this work.Extractions were carried out at different pressure, temperature and flow rate to analyse the influence of these variables on the extraction kinetics and the oil quality obtained.Extraction curves are initially linear with a slope close to the oil solubility value in supercritical CO 2 . Based on these results a mathematical model was successfully applied to describe the extraction curves. Characterization of supercritical crude c… Show more
“…This value is also of the same order as the crossover pressure usually observed in vegetable oils [22,23]. This fact can be also observed in that LCO 2 can be advantageous when working at low operating pressure, since high solubility of fish oil is obtained at low temperature, due to the mentioned retrograde solubility phenomenon, which is beneficial for capital and operating costs [10].…”
Section: Influence Of Pressure and Temperature On The Extraction Yieldsupporting
Liquid and supercritical CO 2 has been used to extract the remaining fat content from rendered fish meal. The effect of pressure (10 -40 MPa) and temperature (25 -80 ºC) on the extraction kinetics and extraction yield has been investigated as well as the effect on the rendered fish meal. The extraction curves are initially linear with a slope close to the oil solubility value in pressurized CO 2 . Based on previous fish oil solubility data reported in the literature, a general equation has been proposed to correlate fish oil solubility data as a function of temperature and density of CO 2 . Fish meal has been * Corresponding author 2 characterized before and after extraction by determining the fat and protein content and its colour. Toxic trace elements have been also determined by ICP-MS in the fish meal showing that most of the toxic elements remained in the fish meal after extraction.Characterization of extracted oil was also performed by determining the fatty acid group composition and some physical parameters such as colour.
“…This value is also of the same order as the crossover pressure usually observed in vegetable oils [22,23]. This fact can be also observed in that LCO 2 can be advantageous when working at low operating pressure, since high solubility of fish oil is obtained at low temperature, due to the mentioned retrograde solubility phenomenon, which is beneficial for capital and operating costs [10].…”
Section: Influence Of Pressure and Temperature On The Extraction Yieldsupporting
Liquid and supercritical CO 2 has been used to extract the remaining fat content from rendered fish meal. The effect of pressure (10 -40 MPa) and temperature (25 -80 ºC) on the extraction kinetics and extraction yield has been investigated as well as the effect on the rendered fish meal. The extraction curves are initially linear with a slope close to the oil solubility value in pressurized CO 2 . Based on previous fish oil solubility data reported in the literature, a general equation has been proposed to correlate fish oil solubility data as a function of temperature and density of CO 2 . Fish meal has been * Corresponding author 2 characterized before and after extraction by determining the fat and protein content and its colour. Toxic trace elements have been also determined by ICP-MS in the fish meal showing that most of the toxic elements remained in the fish meal after extraction.Characterization of extracted oil was also performed by determining the fatty acid group composition and some physical parameters such as colour.
“…Further details of the gas chromatograph method can be found elsewhere. 15 Table 2 shows the fatty acid composition of the fish oil used in this work.…”
Enzymatic alcoholysis of fish oil can produce monoacylglycerols (MAG) rich in polyunsaturated fatty acids at atmospheric pressure and low temperature. Biocatalysis in organic solvents helps to create a homogeneous reaction system for the reactants, ethanol and fish oil. This work presents liquid-liquid equilibrium at two different temperatures (303.2 and 323.2 K) and at atmospheric pressure for two solvent-systems in the ethanolysis of fish oil: Ethanol + oil + tert-pentanol and ethanol + oil + hexane. Experimental solubility (binodal) curves were obtained by the cloud point method and tie-line composition was obtained by density and high temperature gas chromatography (HT-GC). The consistency of experimental tie line data was checked by using the Othmer-Tobias equation. The experimental liquid-liquid data were correlated satisfactorily by the nonrandom two liquid (NRTL) model for activity coefficient calculation.
“…The fatty acid profile of the fish oil used in this work and different MAG fractions has been determined by gas chromatography by following the AOAC method 12 . Details of the gas chromatograph method can be found elsewhere 13 .…”
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