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