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

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also cop~ected<br />

to the pipes leading to the bottom fitting.<br />

A thermometer (0-200 0 0, 0.2°0 divisions) and a thermocouple<br />

measured the inlet steam temperature at the top fitting.<br />

~Jhen<br />

in the cooling cycle the cold water passed t~~ough<br />

a rotameter (Fisher-Porter Fl01~ator Meter (Series 10A27000)<br />

9.4 gallon per minute), and entered the t~nk t~~ough the<br />

same ports used by the steam.<br />

The cooling 1.vater was removed<br />

from the jacket throus-h the second nipple at the top \Alhere<br />

both a thermocouple and a (O-lOOOC, O.loC division) thermometer<br />

measured its temperature.<br />

Figure 4-3 Sh01-JS the piping<br />

layout and the placement <strong>of</strong> the <strong>batch</strong> thermocouples.<br />

Table<br />

1-1_-1 is a sU11nnary <strong>of</strong> the vessel and associated equipment ..<br />

Agit,ation<br />

Four 1 inch baffle s Here welded to a circular frame<br />

v,rhich could be removed from the vessel if desired.<br />

The<br />

length <strong>of</strong> these baffles was 20 inches. Although the baffles<br />

touched the vessel \>

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