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

248
CALCULATED RESULTS
PADDLES - CENTER HEIGHT 7 • .0 inches
93.7% GLYCERINE
Run Diameter h N Npo N Re
N pr KIT{
x Height
Nu
w
( Btu )
(inches x of hr £t.
inches)
2
Heatins.
262 4 • .0 x 1..0 64 lj·32 2.5.0 843 528 6.66
261 4 • .0 x 1..0 112 759 2.01 26.0.0 337 3.99
26.0 4 • .0 x 1..0 15.0 1.016 2.26 4389 3.05 3.32
259 4 • .0 x 1.0 199 1348 2.42 78.09 228 2 •. 49
258 4 • .0 x 2.0 44 ,.01 4.62 868 481 5.86
257 4 • .0 x 2 • .0 132 896 5 • .0.0 2749 222 2.75
256 4 • .0 x 2 • .0 142 961 5 • .05 2478 323 3.51
255 4 • .0 x 2 • .0 178 12.05 5 • .05 4345 25.0 2.72
253 6 • .0 x 1..0 64 433 1.12 667 654 8.25
254 6.0 x 1..0 1.07 723. 1.44 2524 332 4.21
252 6.0 x 1.0 166 1121:) 1.42 .7941 ·182 2.29
251 6.0 x 1..0 189 128.0 1. 52 7392 287 2.93
21:).0 6 • .0 x 2 • .0 69 465 2.84 541 652 8.28
249 6 • .0 x 2 • .0 1.08 734 3.95 2252 288 3.17
248 6 • .0 x 2 • .0 116 1193 3 .L~4 4773 251 2.69
247 6 • .0 x 2 • .0 199 1346 3.67 3756 398 3.44
246 8 • .0 x 1..0 82 554 ·.0.9.0 1658 4.06 5.17
245 8 • .0 x 1..0 1.09 74.0 .0.92 2972 389 4.5.0
244 8 • .0 x 1..0 18.0 1218 1 • .02· 8175 242 2.7.0
243 8 • .0 x 1..0 193 13DB 1.03 6635 38.0 3.lj-4
242 8 • .0 x 2 • .0 92 621 1.77 1516 386 4.81
241 8 • .0 x 2 • .0 149 1DC9 2.22 4537 2.06 2.5.0
24.0 8.0 x 2 • .0 185 1254 2.46 4938 294 2.96
239 8 • .0 x 2 • .0 197 1336 2.45 6672 289 2.3.0