Prediction of batch heat transfer coefficients for pseudoplastic fluids ...
Prediction of batch heat transfer coefficients for pseudoplastic fluids ... Prediction of batch heat transfer coefficients for pseudoplastic fluids ...
2/8 DATA PROPELL:SH3 0.15 P:~RCEN'l' CARBOPOL Batch Weigbt 94.4 Ibs. Clearanc" ~ 10.0 inches Run Diameter RPM 'u'ea 2 Dynamometer 'l'emperature (oC) Time Cinches) (ft. ) Scale T:l;d;ch VIall (min) (lbs) 1 2 1 2 ------ -- Heati~G 341 4.1 372 - 6.20 0.17 47.7 ')7.8 91.7 94.2 2.0 342 4.1 482 6.20 0.21 58.2 1)7.2 91,5 95.2 2.0 343 4.1 596 6.20 0.27 54.0 (;4-,9 f\8.9 92.8 -2.0 3L~4 4.1 766 6.20 0.55 L~9. 2 (-)1.5 82.8 89.8 2.0 353 6.0 113 6.20 0.11 53.8 61.3 95.3 97.2 2.0 35L~ 6.0 315 6.20 0.55 55.G ()6.7 84-.8 91.7 2.0 355 6.0 496 6.20 1.43 53.8 (:'7.1 77.7 88.9 2.0 356 6.0 630 6.20 2.43 55.8 69.0 '7'-1-.7 87.7 2.0 Q2.01~~ 341 4.1 372 6.20 0.17 59.9 53.5 35.2 31.7 4.0 342 4.1 482 6.20 0.21 61.0 53.2 38.2 38.8 4.0 343 4.1 596 6.20 0.27 60.6 52.1 39.8 34.2 4.0 344 /-1-.1 766 6.20 0.55 58.7 1-I-9. l e 40.0 35.3 4.0 354_ 6.0 315 6.20 0.55 66,0 55.4- Le7.0 39.9 4.0 355 6.0 496 6.20 1.43 58.8 1-1-8.2 45.3 37.5 4.0 356 6.0 630 6.20 2.43 64.0 50.8 50.7 41.2 4.0
DATA PROPELJ,SRS 219 CARBOPOL SOLUTIONS Batch Weight 94.4 lbs. Clearance = 10.0 inches Run Diameter RPM Area2 Dynamometer 'remperature COC) Time (inches) (n. ) Scale Batch Wall (min) (lbf?) 1 2 1 2 Heatine; 0.20 Percent CARBOPOL 381 6.0 324 6.20 0.73 43.3 49.7 88.8 91.8 2.0 382 6.0 396 6.20 0.88 37.8 47.0 90.1 92.8 2.0 383 6.0 572 6.20 2.08 51.2 62.1 85.3 90.7 2.0 Cooli!!E; 385-2 4.1 766 6.20 0.55 38.2 34.1 22.7 20.7 6.0 381 6.0 324 6.20 0.73 55.7 49.4 30.9 27.3 6.0 382 6.0 396 6.20 0.b8 ':;6.3 48.7 35.0 29.2 6.0 383 6.-0 572 6.20 2.21 62.1 49.7 43.3 33.8 6~0 0.24 Percent CARBOPOL Heatine; 427. 6.0 500 6.20 1. 58 45.7 52.8 94.3 96.2 2.0 428 6.0 572 6.20 2.08 49.8 57.9 94.9 95.8 2.0 L~29 6.0 650 6.20 2.65 48.8 58.3 88.3 90.2 2.0 Cooline; 427 6.0 500 6.20 1.58 51~ .3 48.7 30.8 27.8 6.0 428 6.0 572 6.20 2.08 56.3 49.2 34.9 30.1 6.0 429 6.0 650 6.20 2.65 52.4 44.8 34.6 29.3 6.0
- Page 180 and 181: 168 TABLE A-4. SLOPE OF "LOG SHEAR
- Page 182 and 183: TABLE 11.-5 RHEOLOGICAL DATA FOR CA
- Page 184 and 185: TABLE A-5 (eollt. ) /12 o . 24;;& C
- Page 186 and 187: '11 The flow behavior index and flu
- Page 188 and 189: i .f.C ·F s o 6 1 6 I
- Page 190 and 191: · . . . " , · . :::11" ': "'" ~ .
- Page 192 and 193: 180 Tke thermal e€l1'!ciluetlvity
- Page 194 and 195: 182 Heat capacity data for 100% gly
- Page 196 and 197: IB4- wkiek ex~resses the aensity e
- Page 198 and 199: 186 Ts - Torque X :: Peree~t 0~ ful
- Page 200 and 201: Phase I Calcu13tiJ~ of Slope of !oG
- Page 202 and 203: 3 REAL). N. ti •• D 4 cN=N E'I'
- Page 204 and 205: ~~-- ~---- --~--~ ~~~--------------
- Page 206 and 207: Phase IV Correlation of Flow Behavi
- Page 208 and 209: 96 HEAT TRANSFER DATA FOR WA'fER US
- Page 210 and 211: DATA /98 Batch \'ieight '" 94 •.
- Page 212 and 213: zoo Run Center Dia!!1ec;er Ri'M Are
- Page 214 and 215: DATA 20l. WATER - TUHBINSS Batch We
- Page 216 and 217: 204- HEAT T'rtANSFEH DATA USED IN C
- Page 218 and 219: DATA ANCHor;: 206 Batch :'Ieight =
- Page 220 and 221: 2.08 Run Diameter RP!'1 Area Dynamo
- Page 222 and 223: DAT_': 210 "i'ADDI,ES 9:5.7'10 GLYC
- Page 224 and 225: 212 DATA PADDLES 0.15 PEHC:::N'r CA
- Page 226 and 227: 211- D!~ 'I'l\. PA-:JDLES 0.20 PERC
- Page 228 and 229: ~;:. 'I'A 3.16 P.;'DDLES 0.24 PEHCE
- Page 232 and 233: DATA DISK & VANE 'l'URBINE \'iATER
- Page 234 and 235: 2.22 DATA Tu.'i:SINES 0.15 PERCENT
- Page 236 and 237: CALCULATION OF HEAT TRANSFER AND PR
- Page 238 and 239: ________________ ~parent viscosity
- Page 240 and 241: ------------------------ -_._------
- Page 242 and 243: ~--~, ~ ---- ---- -----------~-----
- Page 244 and 245: 232 NOMEliCLATURE FOR BEAT TRANSFER
- Page 246 and 247: 2.34- CALCULATED RSSULTS WATER Run
- Page 248 and 249: 2,36 Run Center Diameter h NNu Npo
- Page 250 and 251: 2.38 CALCULAT'ED ~E~:UL'rS ?!ATER P
- Page 252 and 253: CALCULA'rED 1-{E8iiLlJ. 1 S \.;!\.'
- Page 254 and 255: CALC:_:LA'i'ED _12:-)ULTS 24c. ANCH
- Page 256 and 257: CALCULATEDR3SULTS PADDLE - CENTER H
- Page 258 and 259: CALCULATED HESULTS 216 PADDLES - CE
- Page 260 and 261: 248 CALCULATED RESULTS PADDLES - CE
- Page 262 and 263: CALCULATED RE:>ULTS 2. So PADDLf~S
- Page 264 and 265: PADDLES - CALCULATED RE6ULTS CENTSH
- Page 267 and 268: 255 CALCULATED !tESULTS PROPELLERS
- Page 269 and 270: CALCULA'rED RELmL'l'S PROPELLr~RS -
- Page 271 and 272: CALCULATED HESULTS DISK AND VANE ;r
- Page 273 and 274: DISK AND VAI'E .rU~1BINES CALCULATE
- Page 275 and 276: DISK AND VANE '.i.'UR13HiES - CEl'i
- Page 277 and 278: 26S RESULT,:; U:3ED FOR REGRESSION
- Page 279 and 280: of a least squares line can be calc
2/8<br />
DATA<br />
PROPELL:SH3<br />
0.15 P:~RCEN'l' CARBOPOL<br />
Batch Weigbt 94.4 Ibs. Clearanc"<br />
~<br />
10.0 inches<br />
Run Diameter RPM 'u'ea 2 Dynamometer 'l'emperature (oC) Time<br />
Cinches) (ft. ) Scale T:l;d;ch VIall (min)<br />
(lbs) 1 2 1 2<br />
------ --<br />
Heati~G<br />
341 4.1 372 - 6.20 0.17 47.7 ')7.8 91.7 94.2 2.0<br />
342 4.1 482 6.20 0.21 58.2 1)7.2 91,5 95.2 2.0<br />
343 4.1 596 6.20 0.27 54.0 (;4-,9 f\8.9 92.8 -2.0<br />
3L~4 4.1 766 6.20 0.55 L~9. 2 (-)1.5 82.8 89.8 2.0<br />
353 6.0 113 6.20 0.11 53.8 61.3 95.3 97.2 2.0<br />
35L~ 6.0 315 6.20 0.55 55.G ()6.7 84-.8 91.7 2.0<br />
355 6.0 496 6.20 1.43 53.8 (:'7.1 77.7 88.9 2.0<br />
356 6.0 630 6.20 2.43 55.8 69.0 '7'-1-.7 87.7 2.0<br />
Q2.01~~<br />
341 4.1 372 6.20 0.17 59.9 53.5 35.2 31.7 4.0<br />
342 4.1 482 6.20 0.21 61.0 53.2 38.2 38.8 4.0<br />
343 4.1 596 6.20 0.27 60.6 52.1 39.8 34.2 4.0<br />
344 /-1-.1 766 6.20 0.55 58.7 1-I-9. l e 40.0 35.3 4.0<br />
354_ 6.0 315 6.20 0.55 66,0 55.4- Le7.0 39.9 4.0<br />
355 6.0 496 6.20 1.43 58.8 1-1-8.2 45.3 37.5 4.0<br />
356 6.0 630 6.20 2.43 64.0 50.8 50.7 41.2 4.0
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