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Pharmaceutical Manufacturing Handbook: Production and

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Overall U, English units<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

Half pipe<br />

Jacket w/nozzles<br />

–50 0 50 100 150 200 250<br />

Jacket temperature °C<br />

FIGURE 5 Overall heat transfer coeffi cient for 500 - gal reactors. Comparison of alloy half<br />

pipe with glass - lined carbon steel (GLCS). Syltherm is the heat transfer fl uid. ( From ref. 18 ,<br />

with permission .)<br />

Overall U, English units<br />

60<br />

55<br />

50<br />

45<br />

40<br />

35<br />

30<br />

25<br />

20<br />

15<br />

HEAT TRANSFER IN PROCESS VESSELS 151<br />

Syltherm<br />

Glycol<br />

–50 0 50 100 150 200 250<br />

Jacket temperature °C<br />

FIGURE 6 Overall heat transfer coeffi cient for 500 - gal GLCS reactor. Comparison of Syltherm<br />

with Glycol. ( From ref. 18 , with permission .)<br />

3.1.4.3 Pilot - <strong>and</strong> <strong>Production</strong> - Scale Experiments<br />

The relationships shown in Section 3.1.3 are also pertinent to large - scale reactors.<br />

By using different solvents <strong>and</strong> volumes of solvent, pilot <strong>and</strong> production reactor<br />

heat transfer characteristics can be determined from a series of experiments. A<br />

primary limitation, compared to reaction calorimeter characterization, is that a calibration<br />

probe is rarely available. Thus, heat - up <strong>and</strong> cool - down studies, performed

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