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6 N-Acyl ED3A Chelating Surfactants: Properties and Applications in ...

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Alkyl Polyglycosides 9<br />

The Fischer glycosidation may be described as a process <strong>in</strong> which, <strong>in</strong> a first<br />

step, the dextrose reacts relatively quickly <strong>and</strong> an oligomer equilibrium is<br />

reached. This step is followed by slow degradation of the alkyl polyglycoside. In<br />

the course of the degradation, which consists of dealkylation <strong>and</strong> polymerization<br />

steps, the thermodynamically more stable polydextrose is formed substantially<br />

irreversibly <strong>in</strong> <strong>in</strong>creas<strong>in</strong>g concentrations. Reaction mixtures which have exceeded<br />

an optimal reaction time may be described as “overreacted.”<br />

If the reaction is term<strong>in</strong>ated too early, the result<strong>in</strong>g reaction mixture conta<strong>in</strong>s<br />

a significant amount of residual dextrose. The loss of alkyl polyglycoside active<br />

substance <strong>in</strong> the reaction mixture correlates well with the formation of polydextrose,<br />

the reaction mixture <strong>in</strong> the case of overreacted systems gradually becom<strong>in</strong>g<br />

heterogeneous aga<strong>in</strong> through precipitat<strong>in</strong>g polydextrose. Accord<strong>in</strong>gly,<br />

product quality <strong>and</strong> product yield are critically <strong>in</strong>fluenced by the time at which<br />

the reaction is term<strong>in</strong>ated. Start<strong>in</strong>g with solid dextrose, alkyl polyglycosides low<br />

<strong>in</strong> secondary products are obta<strong>in</strong>ed, provid<strong>in</strong>g other polar constituents (polydextrose)<br />

are filtered off together with the rema<strong>in</strong><strong>in</strong>g carbohydrate from a reaction<br />

mixture that has not fully reacted [28,29].<br />

In an optimized process, the concentration of secondary products formed by<br />

etherification rema<strong>in</strong>s relatively low (depend<strong>in</strong>g on reaction temperature <strong>and</strong><br />

time, type <strong>and</strong> concentration of catalyst, etc.). Figure 6 shows the typical course<br />

of a direct reaction of dextrose <strong>and</strong> fatty alcohol (C 12/14 -OH).<br />

FIG. 6 Mass balance of the glycosidation process.

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