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

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DATA<br />

ANCHor;:<br />

206<br />

Batch :'Ieight = 94.4 1bs.<br />

CARnOPOL :::;OLU ~'ION3<br />

C1e8.rilnce = 5.0 inches<br />

Run Diameter RPf\~ Area;? ;)ynHmOr.1eter Tempp.I":--=-.ture CoC) Time<br />

(inches) (ft. ) 0cf11e Batch I'lall \r:lin)<br />

(lbs) 1 c:. 1 2<br />

---------- ... _- ------- ~.-.<br />

0.1 ';, :r'crce!'1t CATrF',O?OL<br />

!!~~tinr:<br />

373 9.0 5B h.20 0.h7 53.2 6'>. C; 8R.8 9/).6 2.0<br />

374- 9.0 97 6.20 1.8": 56.) 68.1 83.8 90.5 2.0<br />

375 9.0 1')8 '.20 ':>.0;) 52.7 G0.? '10.3 82.(\ 2.0<br />

376 9.0 ,'06 6.27<br />

:~ _ 9 'I<br />

:)/·1-.5 GEl.7 69.5 Hl.2 2.0<br />

Q£()ling<br />

373 9.0 5t3 6.20 (J. ;',7 58.6 50. L~ :,8.1 -,2.'> le.O<br />

374- 9.0 97 6.20 1.S'i ,6.5 5'-1.2 '+7.7 59.4 4.0<br />

375 9.0 158 6. ,:0 5.03 59.2 4·6.d 47.5 '>7.2 11-.0<br />

376 9.0 =0(; 6.27 8.9'> ,,6.0 50. '3 5 L I.8 41.8 4.0<br />

0.c.0 re~£ent<br />

Q~RJOPO~<br />

Heo.t:i!l3.<br />

415-2 9.0 .8 38.2 11-.0<br />

Heating<br />

~24 ~~~ceg!_f~~TIQ?OL<br />

1~56 9.0 157 6.20 5.2l~l 50.3 60.8 :-,d. (-) Cj2.1 2.0<br />

455 9.0 186 6.20 6.6:'; 4.c:l.7 61.3 8').4· ClO.l 2.0<br />

Lj·54 9.0 20 L I- 6.20 B.O:S 40.d 54.1 '79.0 8').2 2.0<br />

Cooling<br />

457-2 9.0 138 6.20 3.36 ll-'l. ~~ 42.7 27.8 211-.8 6.0<br />

4·56 9.0 167 6.20 5.28 5'i·O 1+4.3 -3'L5 28. l j- 6.0<br />

,'- r- 'Z<br />

455 9.0 186 6.20<br />

~) .. 8) 60.1 118.7j 42.5 =53.6 6.0<br />

454 9.0 2()L, 6.20 8.0'; 52.U 11-2.1 37.3 )0.7 l) .0

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