| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 203796 | Fluid Phase Equilibria | 2007 | 7 Pages |
Abstract
The present paper reports liquid–liquid equilibrium data for the system refined soybean oil + commercial linoleic acid + ethanol + water at 323.2 K. The deviation between experimental and calculated compositions, using NRTL equation, presented a maximum value of 1.21% and an average of 0.82%. The obtained parameter set enables the simulation of liquid–liquid extractors for edible oil deacidification.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Christianne E.C. Rodrigues, Elaine C.D. Peixoto, Antonio J.A. Meirelles,