Optimization of the enzymatic esterification of diglycerol and lauric acid |
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Authors: | Eva García Flavio Ferrari Tomás García Mercedes Martínez José Aracil |
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Affiliation: | (1) Departamento de Ingeniería Química, Facultad de Ciencias Químicas, Universidad Complutense de Madrid, Ciudad Universitaria, 28040 Madrid, Spain |
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Abstract: | In recent years, a number of industrial applications for lipases in biotransformation of fatty acids and lipids have been
developed. One of the main reasons for this growing interest is the reduced overall catalyst cost owing to the development
of commercially available immobilized enzymes, using polymeric carriers that facilitate recovery and reuse of the catalyst.
Additional benefits for industrial applications include the specificity of the enzyme and the mild processing conditions.
Diglycerol resulting from the dimerization of glycerol may replace molecules such as propylene glycol as the hydrophilic moiety
of surfactants. Also, diglycerol fatty acid esters are useful as biodegradable nonionic surfactants for food, cosmetics, and
pharmaceuticals. In this study, the enzymatic esterification of diglycerol and lauric acid has been optimized in a solvent-free
system. The reaction was carried out in a stirred batch reactor with a vacuum pump in order to shift the equilibrium toward
the products. The commercial lipase Novozym-435 was chosen as the most suitable catalyst, and the initial acid/alcohol ratio
was always 1∶1. The reaction of lauric acid and diglycerol leveled off at equilibrium conversion after approximately 1 h of
reaction. Previous work indicated that only temperature and catalyst concentration had significant effects on the conversion,
and a full two-factorial design has proved effective in the study of the influence of these two variables on the process.
The temperature range studied was 63–77°C, and the range of the catalyst concentration was 0.2–5.8 wt%. Both catalyst concentration
and temperature were found to be significant factors in the esterification process, and their influences are positive. The
effect of the interaction between temperature and catalyst concentration was small. A first-order approach could not fit the
data adequately, and a model that included quadratic effects was required. A second-order model was developed to predict the
yield of ester as a function of the variables. Analysis of residuals showed that the model predicted accurately the acid conversion
over the experimental range considered. This model is useful to determine the optimal operating conditions for the industrial
process.
Presented in part at the 91st Annual Meeting of the AOCS in San Diego, April 2000. |
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Keywords: | Design of experiments diglycerol enzymatic esterification lauric acid optimization |
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