[Luyben] Process Mod.. - Student subdomain for University of Bath
[Luyben] Process Mod.. - Student subdomain for University of Bath
[Luyben] Process Mod.. - Student subdomain for University of Bath
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NUMERICAL METHODS 97<br />
T<br />
Newton-Raphson convergence.<br />
Generalizing Eq. (4.9), we get the recursive iteration algorithm :<br />
where Tn + 1 = new guess <strong>of</strong> temperature<br />
Tn = old guess <strong>of</strong> temperature<br />
f, = value <strong>of</strong>f,,, at T = T.<br />
fi = value <strong>of</strong> the derivative <strong>of</strong>f, df/dT, at T = T.<br />
(4.10)<br />
The technique requires the evaluation <strong>of</strong>f ‘, the derivative <strong>of</strong> the function<br />
f(r) with respect to temperature. In our bubblepoint example this can be<br />
obtained analytically.<br />
AT, = PC;: -<br />
p = x &WT+BI) + (1 _ $ &‘z/T+Bz)<br />
-xA,P, -(l -x)&P;<br />
=<br />
T2<br />
(4.11)<br />
If the function .were so complex that an analytical derivative could not be<br />
obtained explicitly, an approximate derivative would have to be calculated<br />
numerically: make a small change in temperature AT, evaluate fat T + AT and<br />
use the approximation<br />
(4.12)<br />
A digital computer program using Eqs. (4.10) and (4.11) is given in Table<br />
4.2. The problem is the same bubblepoint calculation <strong>for</strong> benzene-toluene per<strong>for</strong>med<br />
by interval-halving in Table 4.1, and the same initial guesses are made <strong>of</strong><br />
temperature. The results given in Table 4.2 show that the Newton-Raphson algorithm<br />
is much more effective in this problem than interval halving: only 4 to 5