Cássia Oliveira | UFSCar - Federal University of São Carlos (original) (raw)

Cássia Oliveira

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Research paper thumbnail of Behaviour of Oryzanol and Tocotrienols during the Rice Bran Oil Deacidification Process by Liquid-liquid Extraction, at (283.2 to 333.2) K

The edible oil deacidification by liquid-liquid extraction is an alternative route to obtain vege... more The edible oil deacidification by liquid-liquid extraction is an alternative route to obtain vegetable oils with low content of free fatty acids. The difference in polarity between the triacylglycerol, the main component of vegetable oils, and the solvent, ethanol, guarantees the formation of two phases and permits the removal of free fatty acids. Phase equilibrium data are important for the design of extraction process. This work presents experimental data for the system degummed rice bran oil + free fatty acids + ethanol + water + oryzanol + tocotrienols, at (283.2 to 333.2) K. The addition of the water to the system improves the heterogeneous area. This effect permits the processing of oils with high free fatty acid contents and reduces the loss of neutral oil. In the present work the effect of temperature was also evaluated on the partition of free fatty acids and of oryzanol and tocotrienols.

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Research paper thumbnail of Liquid–liquid equilibrium data for the system limonene+carvone+ethanol+water at 298.2K

Fluid Phase Equilibria, 2013

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Research paper thumbnail of AnaBioPlus: a new package for parameter estimation and simulation of bioprocesses

Brazilian Journal of Chemical Engineering, Oct 1, 2017

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Research paper thumbnail of Behaviour of Oryzanol and Tocotrienols during the Rice Bran Oil Deacidification Process by Liquid-liquid Extraction, at (283.2 to 333.2) K

The edible oil deacidification by liquid-liquid extraction is an alternative route to obtain vege... more The edible oil deacidification by liquid-liquid extraction is an alternative route to obtain vegetable oils with low content of free fatty acids. The difference in polarity between the triacylglycerol, the main component of vegetable oils, and the solvent, ethanol, guarantees the formation of two phases and permits the removal of free fatty acids. Phase equilibrium data are important for the design of extraction process. This work presents experimental data for the system degummed rice bran oil + free fatty acids + ethanol + water + oryzanol + tocotrienols, at (283.2 to 333.2) K. The addition of the water to the system improves the heterogeneous area. This effect permits the processing of oils with high free fatty acid contents and reduces the loss of neutral oil. In the present work the effect of temperature was also evaluated on the partition of free fatty acids and of oryzanol and tocotrienols.

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Research paper thumbnail of Liquid–liquid equilibrium data for the system limonene+carvone+ethanol+water at 298.2K

Fluid Phase Equilibria, 2013

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Research paper thumbnail of AnaBioPlus: a new package for parameter estimation and simulation of bioprocesses

Brazilian Journal of Chemical Engineering, Oct 1, 2017

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