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Food Lipids: Chemistry, Nutrition, and Biotechnology

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Figure 1 Structure of sucrose polyester (Olean).<br />

granted the original patent for sucrose polyester in 1971, spent over $250 million<br />

over the last 25 years to develop this fat substitute. The original application for use<br />

of sucrose polyester as a food additive, filed with the <strong>Food</strong> <strong>and</strong> Drug Administration<br />

(FDA) in April 1987, was withdrawn <strong>and</strong> modified. But on January 24, 1996, the<br />

FDA approved olestra for limited use in savory snacks (namely, chips, curls, <strong>and</strong><br />

crackers). Before the approval, sucrose polyester was evaluated in over 10 animal<br />

studies <strong>and</strong> in 25–30 clinical trials. The approval of olestra was not without controversy.<br />

The Center for Science in the Public Interest (CSPI), a Washington consumer<br />

advocate group, believes that olestra deprives the body of some of the essential<br />

vitamins <strong>and</strong> carotenoid that may protect against cancer. In 1996, in Iowa, Wisconsin,<br />

<strong>and</strong> Colorado, Frito-Lay, a unit of PepsiCo, test-marketed chips made with the<br />

olestra.<br />

1. Synthetic Approaches<br />

Sucrose fatty acid polyester can be synthesized in the presence or absence of organic<br />

solvent. Direct esterification of sucrose with fatty acid is very difficult. The solventfree<br />

process is widely used for the current production of sucrose polyester (18,22).<br />

The synthesis may involve reactions of the following types:<br />

1. Transesterification. Fatty acid methyl esters (FAMEs) <strong>and</strong> sucrose are reacted<br />

in the presence of potassium soaps to form a homogeneous melt<br />

followed by the addition of excess FAME <strong>and</strong> NaH at 130–150�C. In some<br />

cases, potassium carbonate is added to aid the reaction. The function of<br />

soap is to help solubilize sucrose <strong>and</strong> FAME. Methanol, a by-product of<br />

the transesterification reaction, is distilled off (Fig. 2). The active catalyst<br />

is the sucrate ion generated with alkali metal hydrides. This is a two-stage<br />

transesterification process, <strong>and</strong> up to 8–9 hours may be needed to achieve<br />

90% yield of SPE.<br />

2. Interesterification (ester interchange). This involves reacting a short chain<br />

alkyl ester such as sucrose octaacetate (SOAc) with FAME in the presence<br />

of sodium methoxide (NaOCH 3) or Na or K metal as catalyst (14). The<br />

reaction requires extremely anhydrous conditions to prevent hydrolysis of<br />

formed product, catalyst inactivation, or explosion (when Na is in contact<br />

with water). The temperature of the reaction with Na catalyst is lower<br />

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

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