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 ...
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
PADDLES - CALCULATED RESULTS CENTER HEIGHT = 7.0 inches 249 93.7 :;'::>ercent GL ':,"CL~~INE Run Diameter h 1')" -'Nu x Height ( Btu ) (inches x of hr ~t 2 I • inches) Npo 1'1 'Re N pr K/K w Cooline; 262 4-.0 x 1.0 26 178 2.51 1227 353 0.11 261 4.0 x 1.0 45 308 2.01 3055 288 0.14 260 4.0 x 1.0 62 420 2.26 4193 319 0.20 259 4.0 x 1.0 65 4:1)8 2.40 4235 413 0.22 258 4.0 x 2.0 31 211 4.6» 1041 4-03- 0.13 257 4.0 x 2.0 45 306 4.98 1933 313 0.16 256 4.0 x 2.0 57 387 5.05 2623 306 0.19 255 4.0 x 2.0 71 480 5.03 :S194 336 0.23 253 6.0 x 1.0 23 156 1.13 1286 346 0.10 254 6.0 -x 1.0 39 262 1.44 2496 336 0.13 252 6.0 x 1.0 62 419 1.40 4575 309 0.20 251 6.0 x 1.0 77 523 1. 52 -5418 388 0.25 250 6.0 x 2.0 28 Hi7 2.86 1053 342 0.11 249 6.0 x 2.0 38 260 3.93 1477 432 0.15 248 6.0 x 2.0 63 427 3.42 2820 418 0.22 247 6.0 x 2.0 76 517 3.67 3467 430 0.25 246 8.0 x 1.0 28 192 0.90 1693 398 0.10 245 8.0 x 1.0 44 301 0.92 3608 322 0.14 244 8.0 x 1.0 67 453 1.02 5985 527 0.21 243 8.0 x 1.0 144 976 1.04 15,188 171 0.33 242 8.0 x 2.0 33 _226 1.'15 1687 3[1-8 0.12 241 8.0 x 2.0 56 382 2.21 308L~ 299 0.18 240 8.0 x 2.0 84 569 2.45 4152 3L~8 0.26 239 8.0 x 2.0 90 - 611 2.45 5627 341 0.28
- 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 230 and 231: 2/8 DATA PROPELL:SH3 0.15 P:~RCEN'l
- 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 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
- Page 281 and 282: 269 (0-9 where y "" log NNu xl = lo
- Page 283 and 284: -------------- -.Basi.c "Progr.a.rr
- Page 285 and 286: -----------~---------- -~----------
- Page 287 and 288: --~-------------- ------ ~~ -------
- Page 289 and 290: Modi fi cati onB-foT' ev:alnatj ng-
- Page 291 and 292: constants forco~~~latjQn F --------
- Page 293 and 294: .------~.~~-- ---------------------
- Page 295 and 296: 28.J ENGLISH ALPHABET . - ¢,'"'~-=
- Page 297 and 298: References 2.8S 1. ') L. 3. Lt- •
- Page 299 and 300: 287 56. 57. 58. C:;o ./ / . 60. 61.
- Page 301 and 302: 289 119. 120. 121. 122. 123. 12L~
- Page 303 and 304: 176. 177. 178. 179. 1(30. 181. 182.
PADDLES -<br />
CALCULATED RESULTS<br />
CENTER HEIGHT = 7.0 inches<br />
249<br />
93.7 :;'::>ercent GL ':,"CL~~INE<br />
Run Diameter h 1')"<br />
-'Nu<br />
x Height ( Btu )<br />
(inches x <strong>of</strong> hr ~t 2<br />
I •<br />
inches)<br />
Npo 1'1<br />
'Re N pr K/K w<br />
Cooline;<br />
262 4-.0 x 1.0 26 178 2.51 1227 353 0.11<br />
261 4.0 x 1.0 45 308 2.01 3055 288 0.14<br />
260 4.0 x 1.0 62 420 2.26 4193 319 0.20<br />
259 4.0 x 1.0 65 4:1)8 2.40 4235 413 0.22<br />
258 4.0 x 2.0 31 211 4.6» 1041 4-03- 0.13<br />
257 4.0 x 2.0 45 306 4.98 1933 313 0.16<br />
256 4.0 x 2.0 57 387 5.05 2623 306 0.19<br />
255 4.0 x 2.0 71 480 5.03 :S194 336 0.23<br />
253 6.0 x 1.0 23 156 1.13 1286 346 0.10<br />
254 6.0 -x 1.0 39 262 1.44 2496 336 0.13<br />
252 6.0 x 1.0 62 419 1.40 4575 309 0.20<br />
251 6.0 x 1.0 77 523 1. 52 -5418 388 0.25<br />
250 6.0 x 2.0 28 Hi7 2.86 1053 342 0.11<br />
249 6.0 x 2.0 38 260 3.93 1477 432 0.15<br />
248 6.0 x 2.0 63 427 3.42 2820 418 0.22<br />
247 6.0 x 2.0 76 517 3.67 3467 430 0.25<br />
246 8.0 x 1.0 28 192 0.90 1693 398 0.10<br />
245 8.0 x 1.0 44 301 0.92 3608 322 0.14<br />
244 8.0 x 1.0 67 453 1.02 5985 527 0.21<br />
243 8.0 x 1.0 144 976 1.04 15,188 171 0.33<br />
242 8.0 x 2.0 33 _226 1.'15 1687 3[1-8 0.12<br />
241 8.0 x 2.0 56 382 2.21 308L~ 299 0.18<br />
240 8.0 x 2.0 84 569 2.45 4152 3L~8 0.26<br />
239 8.0 x 2.0 90 - 611 2.45 5627 341 0.28
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