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

211-
D!~ 'I'l\.
PA-:JDLES
0.20 PERCENT CAR BOPOL
Batch ',)eic;ht 9l~.4 1bs. Center Height = 7.0 inches
Run Diameter RPJVj At'ea2 Dynamometer 'I'emperature (oC) Time
x Height (ft. ) Scale Batch \va11 (min)
(inches x C lOs) 1 2 1 2
inches)
Heati!!!l
395 4.0 x LO 556 6.20 0.86 49.3 57.0 95.7 96.3 2.0
394 L~. 0 x LO 626 .,i,20 1.05 ')4.2 1+3.d 89.7 9L6 2.0
397 4.0 x LO 714 6.20 l.l~3 49.3 58.4 92.3 95.0 '2.0
392 1+00 x 2.0 340 6.20 1.n 42.':> 4B.3 90.3 94.2 2.0
393 4.0 x 2.0 412 6.20 1.21 5".2 60.5 92.1 93.0 2.0
"01 L~. 0 x 2.0 496 6.20 2.13 52.2 61.8 9L7 94.2 2.0
390 4.0 x 2.0 618 6.20 2.83 11-2.2 5 1 1-.2 82.3 87.7 2.0
402 6.0 x 1.0 278 h.20 1.11 /11.2 49.3 92.9 9'1-.9 2.0
403 6.0 y. 1.0 376 6.20 2.0? Ij.Fl • Po S;~. Pi '-\;. ': (1';;.7 2.0'
P') ('\
404 6.0 x 1.0 432 6.20 2.73 50.7 61. '5 Do' .0 ')L7 ,-.J
405 6.0 x 1.0 532 6.20 I~ .• ? '} 57.2 68.1 8G.b 0~ -;Jr... '" ,j 2.0
399 c-.O x 2.0 240 6.20 2.1') 51.1 61.] 92.0 95.3 2.0
398 6.0 x 2.0 290 6.20 3.08 38.5 51. 7 8ll'.7 88.8 2.0
400 6.0 x 2.0 342 6.20 4.33 ')(').3 6(').3 8').3 90.4 2.0
401 6.0 x 2.0 370 (').20 5.15 ')3.8 66.2 83.4, g1.1 2.0
411 8.0 x 1.0 163 6.20 1.13 52.5 ')9.5 96.6 97.7 2.0
410 8.0 x 1.0 220 6.20 2.13 37.7 48.8 87.3 91.8 2.0
412 b.O x 1.0 272 6.20 3.33 ')2.7 63.2 90.3 94.3 2.0
413 8.0 x 1.0 358 6.20 S.68 50.4 G1.9 80.7 .B9.2 2.0
407 8.0 x 2.0 130 6.20 1.65 46.3 53.8 95.7 98.1 2.0
406 8.0 x 2.0 182 6.20 3.08 11-8.8 59.8 87.4 90.7 2.0
408-2 8.0 x 2.0 216 6.20 4.48 61.1 70.0 85.7 92.2 2.0
409 8.0 x 2.0 265 6.20 7.1'3 f,2.7 73.9 87.h 93.9 2.0