Lipase-catalyzed hydrolysis of canola oil in supercritical carbon dioxide

Citation
K. Rezaei et F. Temelli, Lipase-catalyzed hydrolysis of canola oil in supercritical carbon dioxide, J AM OIL CH, 77(8), 2000, pp. 903-909
Citations number
19
Categorie Soggetti
Agricultural Chemistry
Journal title
JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY
ISSN journal
0003021X → ACNP
Volume
77
Issue
8
Year of publication
2000
Pages
903 - 909
Database
ISI
SICI code
0003-021X(200008)77:8<903:LHOCOI>2.0.ZU;2-U
Abstract
The effect of pressure, temperature, and CO2 flow rate on the extent of con version and the product composition in the enzyme-catalyzed hydrolysis of c anola oil in supercritical carbon dioxide (SCCO2) was investigated using li pase from Mucor miehei immobilized on macroporous anionic resin (Lipozyme I M). Reactions were carried out in a continuous flow reactor at 10, 24, and 38 MPa and 35 and 55 degrees C. Supercritical fluid chromatography was used to analyze the reaction products. A conversion of 63-67% (triglyceride dis appearance) was obtained at 24-38 MPa. Mono- and diglyceride production was minimum at 10 MPa and 35 degrees C. Monoglyceride production was favored a t 24 MPa. The amount of product obtained was higher at 24-38 MPa due to enh anced solubility in SCCO2. Complete hydrolysis of oil should be possible by increasing the enzyme load and/or decreasing the quantity of the oil subst rate. There was a drop in triglyceride conversion over a 24-h reaction time at 38 MPa and 55 degrees C, which may be an indication of loss of enzyme a ctivity. Pressure, temperature, and CO2 flow rate are important parameters to be optimized in the enzyme-catalyzed hydrolysis of canola oil in SCCO2 t o maximize its conversion to high-value products.