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Prediction of batch heat transfer coefficients for pseudoplastic fluids ...

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<strong>of</strong> a least squares line can be calculated from<br />

a=y-bi<br />

b =<br />

~ (Xi -X) (Yi - fj)<br />

~ (Xi - X)2<br />

(0-3<br />

(0-4<br />

l"fhere x and y are the averages <strong>of</strong> the xi and Yi data values ..<br />

A relationship such as<br />

(c-5<br />

can be rewritten as<br />

log 'I = log K + n log if<br />

(C-6<br />

so that it is expressed in the <strong>for</strong>m <strong>of</strong> equation 0-1, Hhere<br />

y :: log I<br />

x = log 1)<br />

a = log I{<br />

b = n<br />

Thus it can be seen that the use <strong>of</strong> the above regression<br />

analysis can be used <strong>for</strong> many simple relationships, provided<br />

they can be l.vri tten in the <strong>for</strong>m <strong>of</strong> equation C -1.<br />

A computer progra~ <strong>for</strong> solving equation 0-3 and C-L~<br />

described by Eisen (59), Has used as the basic prograrn. <strong>for</strong><br />

calculating the parameters <strong>of</strong> the pOHer law equation and<br />

the temperature dependent <strong>for</strong>ms <strong>of</strong> the p01.ver lay.J as described<br />

in Appendix A.<br />

The computer progrom is given in Appendix<br />

A.

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