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

2S8
CALGUL\'F2D TE&)LTS
PS:OPELLJ:;RS - CLE::ArlAIWE = 10 inches
CA:~IlO?OL
SOLU'rIOl,S
Run Diameter h ~'.:i'~u N Nlie IiPr K/Kw i'-J f1 Nil
- ?o
Cinches)
Re Pr
( Btl)
o}l'"l
hr 2)
ft.
0.20 I'ercent CARBOPOL
Heatint;;
381 6.0 68 :~24- 0.71 607 1412 1.85 153 5005
382 5.0 8'7 23) 0.57 790 1332 1.99 198 5:>05
383 6.0 163 537 0.,-,5 IG75 89L~ 1.55 425 '5524
Cooline;
'585-2 LI· .1 LI·4 147 0.64 959 997 0.82 270 3042
3Bl 6.0 41 1'56 0.71 555 1500 0.72 166 5142
382 6.0 58 190 0.57 896 1162 0.75 227 1,596
383 5.0 112 '569 0.69 1660 903 0.78 L~21 3562
0.24 Percent GJLR30FOL
Heatiw5
427 6.0 71 2% 0.5'l- 622 2122 1.39 131 10097
428 6.0 90 298 C).55 h05 1866 1.3L t 159 3910
429 6.0 124 407 0.65 990 1724 1.2':1 207 8231
eooline;
427 6.0 39 129 0.65 623 2078 0.85 133 9907
428 5.0 55 181 0.55 798 1885 0.87 Iv7 8994
429 6.0 72 237 0.54 950 1806 0.89 200 8587