Abstract
A differential vaporization model is proposed in the present research paper in order to simulate the batch physical refining and/or deodorization process used in the vegetable oil industry.
The fractionate distillation based on the differential vapor–liquid equilibrium of oil systems and the steam entrainment of distillate compounds process are mathematically designed in a differential equation for the vapor pressures and activity coefficients.
Cuvinte cheie
edible oils
physical refining
deodorization
mathematical modeling