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LIQUID-LIQUID EQUILIBRIUM AND KINETICS OF ETHANOLIC EXTRACTION OF SOYBEAN OIL USING ETHYL ACETATE AS CO-SOLVENT

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Figure 1 presents the experimental binodal and tie- tie-lines, and also calculated values of binodal curves and
Table 2: Experimental tie lines for the system soybean oil (w 1 ) + ethyl acetate (w 2 ) + anhydrous ethanol (w 3 ), in  mass fraction basis.
Table 3: Fitted binary interaction parameters of the NRTL model for the system soybean oil (w 1 ) + ethyl acetate  (w 2 ) + ethanol (w 3 )
Figure 2: Kinetic experiments at 298.15 (A), 313.15 (B) and 328.15 K (C) using: anhydrous ethanol (■, Dagostin  et al., 2015a); 95% anhydrous ethanol + 5% ethyl acetate (●); 90% anhydrous ethanol + 10% ethyl acetate (▲)
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