Abstract

The volumetric behavior of ethyl esters and fish oil ethyl esters in the presence of supercritical CO 2 was studied with a newly designed flow apparatus. Pure esters studied were ethyl acetate (C2), ethyl octanoate (C8), ethyl laurate (C12) and ethyl linoleate (C18:2). Fish oil ethyl esters were derived from esterification with ethanol. Conditions were CO 2 at 313.2 K over the pressure range of 0.1–25 MPa and over the full range of single phase compositions. The density data were interpreted in terms of swelling factors, V mix/ V ester. It was found that the swelling factors over the full range of compositions at a given pressure could be made to collapse into a single curve by using weight fraction instead of mole fraction. Further, the Soave–Redlich–Kwong equation of state was found to provide prediction of the swelling factors to within 3.0% average error or correlation to within 1.1% average error. Supercritical CO 2+fish oil mixtures were found to show the same swelling behavior as supercritical CO 2+ethyl esters.

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