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 ...
3 REAL). N. ti •• D 4 cN=N E'I'1 = [·1 SX=Lo. 'SY=W. SXY-o. SX2=,O. Sy2=O. D051=1.N --~---RE·AtS'.~TE:lqp~ SHST. RPtC--------- Z= ~209*RPI'l/D SX2=SX2+X*X 5 SV2=SV2+V*V XBAR=SX/EN YEIAR-SY7EN 'j i ---~------,~-~--- ---------------,5"'0"'o",.-+\ .. , -------------~ --------------:S=-C=-=-O-li 500 500 500 ~. ---- -·--·------~-~-----------;=5-;;:0-;;:O-l 500 .... - ..... -------------1 W=ShST/Z ------------.---------------------------------------~; PUNCH. TEji,P. r.(Pf.1. Z. Vi ----·X- .4343*LOG IZ) Y=.4343*LOGISHST) --,------ -SX=SX+X SY=SY+Y SXY=SXYtX*V 6 CX2=SX*SX/E"! ex,' -:3X*S i ; EO!'" VX2=SX2-CX2 VXy=SXY-CXy d=VXY/VX2 A=YL,AR-8*xaAR C=SXY/Sx2 R= ~------... -, ,--_ .... -_ ... 7 8 S2SX=IEN*SX2-SX*SX)/IEN*CEN-l.) I S2SY-IEN*SY2-~y*SYI)(EN*C~N I.}) YGX=IIEN-l.I/(EN-2.»*CS2SY-d*O*S2SX) SYGX-YGx**.S se=SYGX/I(S2SX*IEN-l.)I**.51 !F(B)9.10.1C ·__ n ---- ~oo ~~~ I' 500 500 I ~~~ I ~oo ( 5'00 ! 50 500 1 500 ' 500 I ----.------------~ 500 500 9 i3A=-B 500 ;,a GO TO II SOo ' ,7 ( 10 BA=8 500 ~'6 --·!·1-·....,.-:s-A"'/"'s"8:r-------------·---- -- 500 15 IFIT)12t!3.13 500 I ,'· 12 TA=-T 500 1~' 12 14 DF 2=EN-2. 500 '\ 500 { ___________ ~~G~O~~T~O---1-4----------------------~-----------------------------------------______ ~5~0~,O~ 13 TA-t 500 ( ,'1 ( SEX- ( !Sx2-Sx*Sx7ENj7 tEN I. I )**.::> ': SEY.=((Sv2-SY*SY/EN)/(EN-l.)I**.S 1 1''-'" xK=IQ**A '76el.____\ __ ~P~U~N~C~H~.~T~E~M~P~.~8~.~.~X~K~----------------________________________________________________________ __ POi
191 A - Leg @f f1uid eonsiste~cy ~dex B IIlII Fl0W behaviGr index D .. Sle~e of logal"ith:m.ie £llet 0f shear stress Versus DF2 - N :: 11 :: RPM (B at PJ:lase I) De~rees of rreeaom Number of data ~oints C@nstamt equal te 2 £leI' set RA :: RPM :: SB ::: SHST ::: SXGX :: TA :: TEl'-1P ::: Xl{ - Correlatien coefficient Rotational speed of impeller bob Standard error in computed B Shear stress (dynes/em,2) Standard errer in Y i T of T test Temperatulte Fluid e~nsisteBey DATA TRe first eard of a. set of data had the values at H, M and D. The l'lext H cards each l:.Lad three values cerres]lo:ading to the temperature, shear stress, and shear rate.
- Page 152 and 153: 140 The average deviation of the me
- Page 154 and 155: 42 tween 0.25 and 0.58. L~~l had re
- Page 156 and 157: 144 transfer coefficients to non-Ne
- Page 158 and 159: 16 of fit and it may t...herefore b
- Page 160 and 161: 148 'tvas insufficient data to eval
- Page 162 and 163: 50 A ::: Apr ... B ::: C p ::: CPr
- Page 164 and 165: 52. Q ::. Average heat transfer rat
- Page 166 and 167: Xc = Function of Reynolds nL:l.m.be
- Page 168 and 169: IS6 G REE:>{ ALPHABET 0 ::: Value o
- Page 170 and 171: 158 coefficient. Thus, for the wate
- Page 172 and 173: 160 , ., I .. : I :. '. • • !.
- Page 174 and 175: 162 I , . I . "I '1 I i I 1 I 1· '
- Page 176 and 177: 64 ncr --~iIluto e torque of the in
- Page 178 and 179: 166 rive different temperatures; ab
- 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 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 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
3 REAL). N. ti •• D<br />
4 cN=N<br />
E'I'1 = [·1<br />
SX=Lo.<br />
'SY=W.<br />
SXY-o.<br />
SX2=,O.<br />
Sy2=O.<br />
D051=1.N<br />
--~---RE·AtS'.~TE:lqp~ SHST. RPtC---------<br />
Z= ~209*RPI'l/D<br />
SX2=SX2+X*X<br />
5 SV2=SV2+V*V<br />
XBAR=SX/EN<br />
YEIAR-SY7EN<br />
'j<br />
i<br />
---~------,~-~--- ---------------,5"'0"'o",.-+\<br />
.. , -------------~ --------------:S=-C=-=-O-li<br />
500<br />
500<br />
500<br />
~. ---- -·--·------~-~-----------;=5-;;:0-;;:O-l<br />
500<br />
.... - ..... -------------1<br />
W=ShST/Z ------------.---------------------------------------~;<br />
PUNCH. TEji,P. r.(Pf.1. Z. Vi<br />
----·X- .4343*LOG IZ)<br />
Y=.4343*LOGISHST)<br />
--,------ -SX=SX+X<br />
SY=SY+Y<br />
SXY=SXYtX*V<br />
6<br />
CX2=SX*SX/E"!<br />
ex,' -:3X*S i ; EO!'"<br />
VX2=SX2-CX2<br />
VXy=SXY-CXy<br />
d=VXY/VX2<br />
A=YL,AR-8*xaAR<br />
C=SXY/Sx2<br />
R=<br />
~------... -, ,--_ .... -_ ...<br />
7<br />
8 S2SX=IEN*SX2-SX*SX)/IEN*CEN-l.) I<br />
S2SY-IEN*SY2-~y*SYI)(EN*C~N I.})<br />
YGX=IIEN-l.I/(EN-2.»*CS2SY-d*O*S2SX)<br />
SYGX-YGx**.S<br />
se=SYGX/I(S2SX*IEN-l.)I**.51<br />
!F(B)9.10.1C ·__ n ---- ~oo<br />
~~~ I'<br />
500<br />
500 I<br />
~~~ I<br />
~oo (<br />
5'00 !<br />
50<br />
500 1<br />
500 '<br />
500 I<br />
----.------------~<br />
500<br />
500<br />
9 i3A=-B 500<br />
;,a GO TO II SOo<br />
' ,7 ( 10 BA=8 500<br />
~'6 --·!·1-·....,.-:s-A"'/"'s"8:r-------------·---- -- 500<br />
15 IFIT)12t!3.13 500<br />
I ,'· 12 TA=-T 500<br />
1~'<br />
12 14 DF 2=EN-2. 500<br />
'\<br />
500 {<br />
___________ ~~G~O~~T~O---1-4----------------------~-----------------------------------------______ ~5~0~,O~<br />
13 TA-t 500<br />
(<br />
,'1 ( SEX- ( !Sx2-Sx*Sx7ENj7 tEN I. I )**.::><br />
':<br />
SEY.=((Sv2-SY*SY/EN)/(EN-l.)I**.S<br />
1 1''-'" xK=IQ**A<br />
'76el.____\ __ ~P~U~N~C~H~.~T~E~M~P~.~8~.~.~X~K~----------------________________________________________________________ __<br />
POi