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

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CALCULATED RE:>ULTS<br />

2. So<br />

PADDLf~S - C!~NT'E'~ E;;;IGHT = 7.0 inches<br />

0.15 Percent CARBO i 'OJ,<br />

Run Diameter h r~Nu N po N Re<br />

l~<br />

x Heir.;ht (~~ )<br />

(inches x <strong>of</strong> },:r ft. 2.<br />

inches)<br />

I<br />

i\jK Nil l~ 11<br />

, Pr w ~'Re Pr<br />

geatigg<br />

345 4.0 x 1.0 92 0:-05 ~.6J) 760 344 2.54 "359 729<br />

346 4.0 x 1.0 1'52 ll-3/+ 1.Lf8 2~,4 2fA 2.04 \S86 546<br />

3 i l'7 4,.0 x 1.0 17'7 581 2.22 2fi6R 2'55 1. 9 1 + 1284, 4-87<br />

348 4.0 x 1.0 221 72H c.:";, )494 C52 1.'78 1664 487<br />

349 4.0 x 2.0 137 LI51 4.17 81'7 :;;'Oi:; 1.9,8 '594 636<br />

350 4.0 x 2.0 175 ')71+ I~,.EA 1413 262 1.86 ;:'86 5':)9<br />

351 4.0 x 2.0 2'50 7')1 5.48 2707 210 1.f,6 1333 425<br />

352 4.0 x 2.0 2')3 965 5.59 3149 229 1.61 1511 47B<br />

357 6.0 x 1.0 83 277 1 . I. IA- 521 525 2.98 2:;;'

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