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1 ci 0 Ilc (i) s_ri P4 4) •,-1 0
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ACKC’bJLED3E.:ENTS should like to
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46 iixperimental Results 461 IntroJ
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APPNNDICES 1. PHYSICal PRSPHTIES Oi
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the major unresolved problem in hea
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and time, fouling factors are usual
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o F-I 0 U J ,ij cn J ‘I—I F3 Fl
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—5— vary from less than 1 per c
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2.2.3 Solubility refined paraffin w
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-.9— whica is well novc condition
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— -ii — deposit. Tronov statej
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— 13 remain in solution and the p
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- iuctoov and dorov concluded hat t
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— 17 — a deporsiion ce:Ll in a
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— 19 - toat sur:ace. hjsima.a ot
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— 2 - S * .. -, ‘.: ,- - .-,-
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and surface proueriez reapectlvely_
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- 25 - loading to a random process
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y - F’J CD:’ C) x— Dcpoit thi
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0 C 15O— 200 From ref 2 of wax eo
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0 o3 Tb 3D 0•0 L D 2 •O— Fg.2
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2 I In 0 Tot -D -D U 16H 16 20, In
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C CE) CL) CE) () .: rJ\: - . c: CD
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400 function of roughness factor. m
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— 2o — 3. i3:\CGRDU ND TO TI PR
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3.5 Conclusions decreases At the in
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L - A sz: CF Fo:;:NG BY SOLUTIONS O
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was designed to cut off the steam s
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• saLLy measures were tacen. oa:D
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— 34 .4 ‘mrii:ntal Solution The
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sections were ke-:t the same. fosi:
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sectaon 4- at eajt tests sections h
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These fluctuations were not reduced
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ii ID XXX 9 C-) 0 (N x S x xx< 7r-
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12— -; 11L. s 10E - 9: ‘3) 0 Ru
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(1) U) C’) C) Cl) It) 0 0 0 0 ox
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f-iq. 1.0-3.5.— Hecit trcinsfcr r
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I--i Fig. f.6.3.7. I ;ut transfer r
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0 C’) R — [feat transfer resist
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characteristc does exist and is tyt
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The ziuewor in the circulation syst
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The calibrations o the tesperature
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the solution and water o::a;es thro
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‘-- 5,5 wocrinentsl Resuts with f
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two hours, the deposits were observ
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wcr: on ara:zic: c.eposc.tion consi
- Page 93 and 94: -- II 1 L1 SOLUIIOIJ C;IFCU1_/:[ION
- Page 95 and 96: SCAR FE 1 DEPOSITION PLATE - - 0 C)
- Page 97 and 98: M—AMOUNI DEPOSITED (mg) T1 0_i c)
- Page 99 and 100: C) 0 0 0 Li.] CD - 3 0 3 0 h Iii (E
- Page 101 and 102: - II -fl M—AMOUNT DEPOSITED (rng)
- Page 103 and 104: 91 9) :< C) --z 9] mc-) .;J -i ru
- Page 105 and 106: .1 1• ci E 0 Ci) c) — nj
- Page 107 and 108: - . O, O, I— —,-, fouling studi
- Page 109 and 110: profiles at different Reynolds numb
- Page 111 and 112: L Run . (°c) used to calculate tem
- Page 113 and 114: Due to a concentration gradient the
- Page 115 and 116: 1 I C. (1.2.2.2 \1L. I .OC[FY V [A[
- Page 117 and 118: V 40 - 0 C—, lt! -— o. ---—-
- Page 119 and 120: Li FIG. G.2.3./. TEMPERAI URE v RAD
- Page 121 and 122: — 1 7.0 0 --Tc.=10.0°C 50 140
- Page 123 and 124: — -- — -——— — -—Tb =
- Page 125 and 126: Z_o_—o-- 50 l0 - yX—--X— —-
- Page 127 and 128: I:302 00 50 Ito -0——— ---—-
- Page 129 and 130: I 50 ;) 30c’/ / C —------------
- Page 131 and 132: FIG. 6. 4.1. AN IDEEAL TEMPERATURE
- Page 133 and 134: — 63 — 7. DISCUSSIOI 7.1 Introd
- Page 135 and 136: — 65 — through it decreases gra
- Page 137 and 138: For breakdown and removal to occur
- Page 139 and 140: — 69 — the large fouling studie
- Page 141 and 142: Increased flowrate and temperature
- Page 143: — 72 — 8. ICOi’NDATTCNS It is
- Page 147 and 148: :0 e = Roughness factor Cp = Heat c
- Page 149 and 150: + = Average velocity at centre of t
- Page 151 and 152: Siid
- Page 153 and 154: 17. Nazee, W.M., “Modern Petroleu
- Page 155 and 156: — 81 — 46. Coulson, J., Richard
- Page 157 and 158: i S-i Ti .1” 0 -P -‘‘ •) 0
- Page 159 and 160: — - 5 The viscosity of paraffin w
- Page 161 and 162: — A5 — ..-6 ThD-1 DQactiv1r Thc
- Page 163 and 164: (:) rr 0 Ill U, . CD
- Page 165 and 166: 0 : 0 4-) ri () 0 (‘C 0 “C C’
- Page 167 and 168: — A9 — Table Ai.2.4 Cloud and o
- Page 169 and 170: — A91 — parafi’in w, it was a
- Page 171 and 172: )< 0 0 -H rn rn t - >< rn — o m F
- Page 173 and 174: The pressure transducer was calibra
- Page 175 and 176: — A16 —. Table P.3.2 Pressure t
- Page 177 and 178: - AlS - Table A33.2 Calibiation con
- Page 179 and 180: C C PROGRtt’ NAMF TUEEX J.S.GUOMU
- Page 181 and 182: C C 0 11 = 1K I — T D T 2 -=1K o
- Page 183 and 184: 11.17 7.40 7.65 34.30 33.50 9.5 0.6
- Page 185 and 186: RUN Aq-3 TIME ThI T0 TKI TKC DPK CP
- Page 187 and 188: RUN AIC—’i TIME TWI TC TKI TKC
- Page 189 and 190: 11.03 8.8C 9.8C 43.40 42.00 6.3 0.5
- Page 191 and 192: TINE ThI TWO TKI TKO 00K CPU OPT V
- Page 193 and 194: 16.08 6.6C 8.2C 44.60 42.80 25.5
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. 13.92 6.7C 7.cC ‘t2.8C 41.30 19
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42.15 6.4C 7.CC 42.80 41.00 7.3 1.0
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RUN C1—14 TIME TWI TWO TKI TKC DP
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RUN C2—15 TIME TiI TWO TK! TKC DP
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RUN C3—lé TIME TI TiC TKI TKO OP
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13.08 6.50 7.70 38.0 37.40 1.1.5 0.
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TIME TWI TC TKI TKC DPK CPW OPT V C
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163.17 6.50 7.C 38.OG 37.’0 9.0 0
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163.25 6.50 7.1C 38.70 37.30 3.8 0.
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RUN C1C—21 TIME ThI TWO TKJ TKO D
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RUN D1C—22 TIME TWI TC TKI TKC OP
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against a standard thermometer, was
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— A22 — Table A5.1 Calibration
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( C) setting Terorature Controller
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— A26 — APPENDIX 6 EXPEPINENTAL
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— A28 — Table A6.3 Th.n D2 Time
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-. A30 — Table A65 Iun D4 Time (m
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anoieter Flowrate — A32 — Table
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L U e;rression: / be used. diffusiv
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— A36 — A74 Velocity Distributi
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= y y + by iteration. dy’ + (2) C
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—A40— A8.2.5 Calculation of Phy
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— A42 — To evaluate equation f7
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30 - A44 — 85 Cornouter Calculati
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2 2.00 27 12.93 74 I 15.73 1 1.00 2
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C C C C GOTO 60 0 UtP=UP’USTAR Y=
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C C C. SUPROUTINE FF L11:NS1C’N F
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..RIT2(6,%0) VLSR,VISBS1 50 EORAT(1
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C C C C C C SUROUTIE FLUX REAL L,Lt
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- V C C .URPUrINE UPROF DLMNSIQN FY
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C C C SJtcLiJTINE TPC1F C LIfr:NSIL
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INPUT DATA AND FRICTION FACTOR TKI
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YP UP TP Y U T VIS rc CP PR 1.00 1.
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VP UP TP Y U T VIS TC CP PR 77.00 1