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

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<strong>10</strong>.4 EXAMPLES OF APPLICATION OF KINETIC MODELING<br />

<strong>10</strong>.4.1. Kinetic calculations<br />

Two examples highlighted, are based on simulated model systems (Saguy and Cohen,<br />

1990) describing a nonenzymatic browning reaction (Table 6; Figure 9) and thiamin<br />

retention (Table 7; Figure <strong>10</strong>). The data was generated assuming <strong>the</strong> values <strong>of</strong> <strong>the</strong> energy<br />

<strong>of</strong> activation, E A /R, <strong>the</strong> rate constant defined at a reference temperature, k ref and <strong>the</strong> initial<br />

concentration A o . A random error <strong>of</strong> +/- 5% was introduced to account for realistic<br />

experimental conditions and error. It is worth noting that in both examples, <strong>the</strong> reference<br />

temperature, T ref , was chosen as 300 K. As pointed out previously, this transformtaion is<br />

important for improving <strong>the</strong> stability during numerical integration and for nonlinear<br />

parameter estimation. The transformation is also recommended since <strong>the</strong> parameters are<br />

highly co-linear and are not easily regressed directly (Cohen and Saguy, 1985; Haralampu<br />

et al., 1985; Nelson, 1983).<br />

Linear and nonlinear subroutines were utilized to derive <strong>the</strong> regression<br />

coefficients and analyses (BMDP1R and BMDPAR; Dixon, 1989).<br />

Figure 9.<br />

Nonenzymatic browning <strong>of</strong> a model system as a function <strong>of</strong><br />

storage temperature (zero order reaction).<br />

53

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