Supercritical extraction with pure and modified CO2 has been used for the fractionation of waste frying oil at different temperature and pressure conditions (25−80 °C and 300−400 kg/cm2). The cosolvents used to modify the CO2 behavior were ethanol, methanol, acetone, and hexane. They were selected because of their capacity to form hydrogen bonds. Both extraction rate and oil yield were larger under high density conditions (high pressure and low temperature). Further, when cosolvents were used, higher values of both variables were attained at softer operating pressures. Regarding the effect of cosolvents on these variables, it was found to follow this order: ethanol > methanol > acetone > hexane. The relative separation efficiency (RSE) of triglycerides (TG) from polar compounds with molecular weight higher than triglycerides (HMWC) was not greatly dependent on the operating conditions (pressure, temperature, cosolvent type, and cosolvent concentration). However, better values of the separation efficiency ...
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