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the handbook of food engineering practice crc press chapter 10 ...

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Lund, 1985). The standarized residuals should be randomly distributed around zero and<br />

usually within -2 and +2. Any data that generate standard residuals outside this range are<br />

possible outliers.<br />

An alternative procedure to linear regression for <strong>the</strong> calculation <strong>of</strong> k is <strong>the</strong> point<br />

by point or long interval method (Margerison, 1969; Lund, 1983), in which each data point<br />

is an independent experiment with respect to zero time. The value <strong>of</strong> k is calculated as <strong>the</strong><br />

average <strong>of</strong> <strong>the</strong> n individual slopes.<br />

Labuza (1984) showed that one gets similar value<br />

ranges for k from <strong>the</strong> two methods. A minimum <strong>of</strong> 8 data points is recommended by<br />

Labuza and Kamman (1983) for reasonably narrow confidence limits in k within <strong>the</strong><br />

practical and economic limits <strong>of</strong> most experimentation.<br />

In some cases higher or fractional order models are clearly indicated by <strong>the</strong><br />

experimental data. To determine <strong>the</strong> apparent order m, two methods can be alternatively<br />

used. As mentioned before, different values for m can be assumed and <strong>the</strong> fit <strong>of</strong> <strong>the</strong> quality<br />

function for m≠1 (Table 1), tested. A second method is to allow m as a parameter and run<br />

a nonlinear least square regression on <strong>the</strong> equation to determine <strong>the</strong> order that best<br />

conforms with <strong>the</strong> experimental data. For example, it was found that second order kinetics<br />

best described <strong>the</strong> oxidation <strong>of</strong> extractable color pigments from chili pepper (Chen and<br />

Gutmanis, 1968). Autoxidation <strong>of</strong> fatty acids in presence <strong>of</strong> excess oxygen is best<br />

described with a 1/2 order model with respect to <strong>the</strong> fatty acid concentration (Labuza,<br />

1971), whereas hexanal production from lipid oxidation is shown to <strong>the</strong>oretically fit a cubic<br />

model (Koelsch and Labuza, 1992).<br />

As has been explained before, <strong>the</strong> developed <strong>food</strong> quality loss functions are<br />

based on <strong>the</strong> stated assumptions and do not necessarly reflect true reaction mechanisms.<br />

In case for which <strong>the</strong> assumptions are not applicable or <strong>the</strong> actual mechanism is very<br />

complex due to side reactions or limiting intermediate steps, equations (9) and (<strong>10</strong>) may<br />

not sufficiently model <strong>the</strong> measured changes. One approach in this case is to develop a<br />

15

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