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

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182<br />

Heat capacity data <strong>for</strong> 100% glycerine is reported at many<br />

temperatures (49, 95, 1~.3)<br />

and can be expressed as<br />

Cp(lOO% GLYCERINE) :: 0.535 + 0.00132T<br />

<strong>for</strong> C p<br />

in Btu/lb.op <strong>for</strong> T in degrees Centigrade.<br />

(A-16<br />

Substituting<br />

the above value <strong>for</strong> water and equation A-16 <strong>for</strong><br />

100%, glycerine in equation A-1S yields<br />

Cp(SOLN) :: (1.003) (0.063) + 0 .. 937 (0.535+0.00132T)<br />

(A-I?<br />

or<br />

Cp (93.?% GLYCERINE) ... 0.565 + 0.0012LI·T<br />

(A-IS<br />

with an estimated accuracy <strong>of</strong> ± 3 .. 0 percent.<br />

The <strong>heat</strong> capacity <strong>of</strong> Carbopol solutions <strong>of</strong> approximately<br />

the same concentrations used in this thesis Here reported<br />

by Ferment (63) to be the same as <strong>for</strong> water.<br />

Ferment<br />

estimated the accuracy <strong>of</strong> his measurements to be ± 5.0 percent.<br />

Thus the <strong>heat</strong> capacity <strong>of</strong> the Carbopol solutions vIas<br />

1.003 ~ 5.0% Btu/lb.Op.<br />

DENSITY<br />

Values <strong>of</strong> the density, f ' <strong>of</strong> water at various temperatures<br />

are reported by Badger and McCabe (10).<br />

The data<br />

l,.Jere ass1Lrned to be represented by an equation <strong>of</strong> the <strong>for</strong>m.

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