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Food Lipids: Chemistry, Nutrition, and Biotechnology

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Solid:<br />

Liquid:<br />

SSS, 33.3%<br />

OOO, 8.3%<br />

OOL, 24.99%<br />

OLL, 24.99%<br />

LLL, 8.3%<br />

The segregation of saturated fatty acids into trisaturated species is necessarily<br />

accompanied by a corresponding tendency for unsaturated fatty acids to form triunsaturated<br />

species [47].<br />

VIII. KINETICS OF CHEMICAL INTERESTERIFICATION<br />

R<strong>and</strong>om interesterification is usually conducted until equilibrium has been reached.<br />

There are many conflicting reports in the literature concerning interesterification reaction<br />

rates. Coenen [41] stated that once a sufficient concentration of catalyst in<br />

solution had been reached in the reaction mixture, the actual interesterification reaction<br />

was extremely fast, requiring only a few minutes, unless operations had to<br />

proceed at very low temperatures. The kinetics were modeled in several ways to<br />

support this theory. The first example was a model system consisting of short chain<br />

fatty esters (C8, C10) of ethylene glycol (Fig. 9). The induction period was long,<br />

yet the reaction itself was rapid, even at 32�C. In the second example, interesterification<br />

of palm oil was evaluated using solid fat content determinations (Fig. 10).<br />

The reaction rate was faster at higher temperatures. These data confirm that an activation<br />

period is indeed required <strong>and</strong> agree with Weiss et al. [24] <strong>and</strong> Rozenaal [11],<br />

who reported that the catalyst formation phase was longer than the interesterification<br />

Figure 9 Theoretical interesterification kinetics of glycol esters of C8 <strong>and</strong> C10 as a function<br />

of time <strong>and</strong> temperature. 42�C (�); 37�C) (●); 32�C (▫). (Adapted from Ref. 41.)<br />

Copyright 2002 by Marcel Dekker, Inc. All Rights Reserved.

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