P C)’ C) C) c-U ci C)’ C) C) CL I-’ F—) ) C) It’ c-I’ U) It)’ C,) CD Cl) C) C) C) CL c-U C) p. Cn :: o i-’• :i CL F-’ (ti F) ‘,J1 Ij ç’z, c CD ‘.31 CL C CC) ci 9,‘ I-” F-) C’)- I” H U) (_) iL F) F Ii C) Cl) C) ct ci’ CL) U) C’ CD L’5 0 Ci’ c-’, i-l C) H1 d ci’ 0 F)) FL’ L’S L’5 F)) F)’ c-I’ ci’ ‘—CL L” L’, c-i’ (C) 1-” C) CD ‘-U ‘-S )!Z Cl) (C’ F’ O C) H CL) CS C) c-i’ c-i’ CD H’ “U o C) Si U) L’5 )). F):) ‘c-S c-U CL) C) C) U’) —, Cl) — o CL) H • c-I- CL C) C’) CD [‘0 P p o ‘ C’, H p ci C: C- ‘S ) -,‘ I’’ F’ I-.,, (LL ci- F” F’5 (,, C’ C,’-’ C) C)’ C) C’ C) 1- 1’ CL) F” I” I” I” U) C. p ‘ 1 o 0 ‘,: F’, t, P• p c-U c,’ C’) — (_., ci’ C)- C) I C,, (‘1 1L C,’ ‘Ci Ci’ I; ‘-S c-i’ (,, I’’. C)’ (Li P Ci’ Ct’ C p p cl c-I- i.i. — C”,, ‘S C”) : c, c’ I---’ C) 1’ p ci U) I:) :-- c-, C: (U p S C) p IL U’ C, ‘ (1 V. I,. p. Q F I,,; C) FL’ IS 1; 0 F” C’) l’• F’ ‘-: : i C,’ CD .“ i_i • :. C) CL’) ‘1,_I “ r ct’ C,’ CL) 15 ci 0 CL,’ F’, Ii. F’ F” F” U-’ ‘ Cl ‘L C” 15 p. C) C) C) Cl (Li F’ P (D F’, C)’ CL’ C C,:: U’ C,) ci F’ F) C)’ C:’ c-i’ (U I” 5’,t C) C,’ (ii P CL (CL P [‘: c” C) F) CL) U) ‘CS ( p. (, o C) p. (ci C) ‘,; ci- C) C, CD Cj CL) is F’ C) ) U) < 0 CL C,- I C,) F’ (I, UI C .-“ . .“ Ito N ci, cit ci, C” .‘‘ .—.- C) J, 0 [‘0 N ri) -‘.D C) (5-i • I S [‘0 \C) D C) ro Ito -..D 0-i • ci o Co r’j C)’i • 0’, F) c-U H CD c-I ._,_% __i .- .Il ‘Ui • C .P’ • .— C) CX) ___i _)i ‘ji -Fl- f S C I o ‘.0 . p. C) S ci I’--I (CL ii p ‘C_i C)) C Cfl ci’ 5 0 FLI j.-L c F’ 1- ci “ p. oCLO C) C—, 0 C’) c-I’ H (DO P 0 1—’ iJ C’) CD (DL’ c-I’ ‘, p. F) F’ 0’) C) (Dpi I” ci’ ‘“CL) I’ Oj C)) C-) \,,fl El 1.1 UI CL V• C) 0 :;‘ CD ,) CD Ei P. \Ji ‘U ‘U 0 ci’ Ct: 0 CD ‘-5 0 c-I ) 0 C)’ ci- H ‘S Cl) Ii P• 0 “-5 F’ P CL) (CL CC) 0 ‘S I-.’ i-s F’ It-) Ct’ L C) c-i F-) c-I’ I-” F’- CD cU C) (CL . I’S 0 F’ ‘fl {‘4 1’ “S FL) o C’) $)‘ F’ 0i 0 I F’pi ci’ ci’ Cl) 5)5 CL) i C)) C i-L 1 c-U ‘-5 CD F, F’, ‘-I. C) ‘IC) U) I”. F’S F-” Li CL) “-S C,) C) o 0 PCD CL) ci’ (I, \J’) U) p p pi F) Ci) ci p I--’ ‘S CD I--I. I” F’ “5 C) S ci’ F) Ii c-I ci ‘5 CD CU II Cu 1-1 Cl) F-’ i-U c)’ F’- CC’ “U F1 ‘S “5 o F) 1.-I. i-( 5 C)’ ‘U’) C’) F’ S I--S ci’ C) CD F-’ U) C) N C) F’ F’ I-S U) 6-i C) p C) 0 ci- - D ‘-S U U) Ct’ F)) ‘i_I) c-I’ . c’l f’ C!) CD I(,) ‘(,) c-; l--’ C) C) o 0 F-, P• I ‘ ci’ I—’’ I-” c-U 0 1” F’ F-” Ii H £ C) f-I. c- 5 F’ H’ 10 F’ C) C) 6j CX) P C’)’ C) U- CL’ H C F’ “S ci’ CU CC’ C) (CL C< I’S 0 ii c-U ci- i,,j \,J1 :‘, H’ C) 0 C)’ N C F’ Cl) Cl) CO Q’ H1 1-5 ,-,‘ P c-U F’-’ F-Li 10 C) F) C)) F) H H I-’ I’) p o p C’ ,-,_5 c’ C) C) —‘ U (CL F’ c-i- c’i- F-D “—‘ F-i ‘-S F’ 0 F’ C)’ Fl’ ci’ “S p) C:, ci’ I- U) c-CL C) F’ C-’ C) ci C) CD U, L’S C) 0) Fl’ ‘S CD U) H C C) 1-J CD F’ C’) i) C) Cl) ci’ 0 o ,“ CD ci’ C C) F’ CC’ C) CC’ F’- c--I F’ F’ “S H CD U) ,j ‘U) o 0 “U P ci- C:, ro )i ‘ C) ., C,L, C)’ C’) 1’ Cl) CD Cl) F’ 0 C)) L’5 p. )‘ Ci ‘S C)) c-I’ c, o -‘ cii “U ‘ < F’- “S C) ,‘ CL’ 0 F’ CL) i-5 C’: ‘-‘El I,.) o F’-’ C) F’ F’ ‘-‘S F’ 0) 1” F’ CL C’) C)’ C) c-U C) F” Ui CL) F’. F’ ()‘ p. ‘ P CD F)’ Ct’ p F-’. f-1. CD P r” F-’ CD C) C) C) CC) I--’. Ci) I-:, c-U :‘ U) “5 c-i- p c-U Cl) It) CD F) F’ C) F) C) ci’ C) c-U H H U) 0 C) I” c-i’ 0 IL, Cl) U) CL) cl ‘-ci “S ci- ci’ CLI 1-’ I Cl) F)’ P H1 I,) C) C) )E: CD 15 o (CL p .,‘) ci- c, CC) U ‘ o CD ‘-5 F’ C) C’) p Ci H CD I” ci- I-’ C’) F C)’ F’, ci’ ci CD bi C n 0 ‘5 S Ci’ F’ (U F’ 0 CD I- IL1 F’ CD C 0 p “5 C)’ C) CL) is
wcr: on ara:zic: c.eposc.tion considered this ana usea an oxc.daton irJic.bitor i:: nis a fact a fectiag the coaparability of the ecerisenta results. Oxatzoa ci tac parazzia <strong>wax</strong> ifl kerosene SQiutloas CO OC derositia frcr.: a rcsh so.ion was, in sorie cases slighty he couc oi — 53 — .‘&ien the solution circulation systea was eniptied <strong>and</strong> &eaneó. ac. on ctc.oa. ci <strong>wax</strong> deposited could also be deternined by urea evaporating -h solvent under vacnurc or passing warn dry air over dposted <strong>wax</strong>. The iepcsi;ion plate could possibly be dried br The use of a better aethod to deternine the anount of migxzt tac recuctc.on Zn coatancaants present in solvents ana wac:es znnt c.ncrease ;:..e conparaJc._c.ty oz tac ecpeI’iaenuai resn;s,, as The use of an oxidation ibitor <strong>and</strong>/or a nitrogia blanket cible results. recuce tie proJ_en o: evaporation o: igat encs. ae use Di c.Ec. The use of a solvont with a closer bo:lang range won_c zuture wor.c., are ;ae :oowang: exists for c.ntroveaen;s .zcng the jtCSS to ce ccnsc.cerec in any Although the exuerimental systera produced results shcwing 56. :teccencatifl3 the <strong>paraffin</strong> <strong>deposition</strong> in one way or another. bottorc of the solution tank. These impurities probably affected LC1 roint fuly refined <strong>paraffin</strong> <strong>wax</strong>es would give nore reirocu— the asy::.Dtotic behaviour of <strong>paraffin</strong> <strong>deposition</strong>., considerabe scope i:aurc.ties iron the kerosene <strong>and</strong> the <strong>paraffin</strong> <strong>wax</strong> were foarco. on the greater than at _a-er tiaus altnoug’n no difereace was cetectec. in
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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
- Page 39 and 40: 0 C 15O— 200 From ref 2 of wax eo
- Page 41 and 42: 0 o3 Tb 3D 0•0 L D 2 •O— Fg.2
- Page 43 and 44: 2 I In 0 Tot -D -D U 16H 16 20, In
- Page 45 and 46: C CE) CL) CE) () .: rJ\: - . c: CD
- Page 47 and 48: 400 function of roughness factor. m
- Page 49 and 50: — 2o — 3. i3:\CGRDU ND TO TI PR
- Page 51 and 52: 3.5 Conclusions decreases At the in
- Page 53 and 54: L - A sz: CF Fo:;:NG BY SOLUTIONS O
- Page 55 and 56: was designed to cut off the steam s
- Page 57 and 58: • saLLy measures were tacen. oa:D
- Page 59 and 60: — 34 .4 ‘mrii:ntal Solution The
- Page 61 and 62: sections were ke-:t the same. fosi:
- Page 63 and 64: sectaon 4- at eajt tests sections h
- Page 65 and 66: These fluctuations were not reduced
- Page 67 and 68: ii ID XXX 9 C-) 0 (N x S x xx< 7r-
- Page 69 and 70: 12— -; 11L. s 10E - 9: ‘3) 0 Ru
- Page 71 and 72: (1) U) C’) C) Cl) It) 0 0 0 0 ox
- Page 73 and 74: f-iq. 1.0-3.5.— Hecit trcinsfcr r
- Page 75 and 76: I--i Fig. f.6.3.7. I ;ut transfer r
- Page 77 and 78: 0 C’) R — [feat transfer resist
- Page 79 and 80: characteristc does exist and is tyt
- Page 81 and 82: The ziuewor in the circulation syst
- Page 83 and 84: The calibrations o the tesperature
- Page 85 and 86: the solution and water o::a;es thro
- Page 87 and 88: ‘-- 5,5 wocrinentsl Resuts with f
- Page 89: two hours, the deposits were observ
- 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
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Increased flowrate and temperature
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— 72 — 8. ICOi’NDATTCNS It is
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EEfiDN2WON
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T TemDerature T = Average temperatu
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= :ieat eddy dfusivity = Xoent eddy
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in Exchar.ge: Tubes”, Chem. Engr.
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Oil Gas J., 58 (38), 87—91 (Sept.
- Page 156 and 157:
U U F--I C) (f
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The o1ubi1ity of 5i/54°Cparafin wa
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— — .‘.ti+ c:Lic gravity The
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In section Al .4 the auount of pcra
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0 •) X S (N U ‘0 -° CD c-) ( -
- Page 166 and 167:
I-] H — C C) p 0’ H 0’ H CD C
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fully refined paraffin wax in keros
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— A12 — The cloud point decrens
- Page 172 and 173:
— A3 — Tnble A2.1 Ca1culccd c i
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calibration constants are given in
- Page 176 and 177:
— Al? — Table A3.3.1 Calibratio
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— A19 — APPENDIX 4 THE PRDGR’
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C NC = C C REiCS EACH SET OF RE[iJC
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13.42 7.40 7.SC 33.90 33.10 13.8 0.
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TIME TI TO TKI TKC DPK EPW DPT V CF
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81.15 7.45 7.7C 33.40 32.70 30.0 0.
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RUN A1C—4 TIME 1WI TWO TKI TKC DP
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RUN 82—6 TIME TiI TC TKI TKC OPK
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TIME TWI TWO TKI TKC OPK CPW OPT V
- Page 194 and 195:
RUN B7—1C TIME TWI TWC TKI TKO DP
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RUN B9—12 T V’E ThI TWC TKI TKC
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RUN C1—1t T1’E IWI TWO TKI TKC
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PUN C2—15 TIME T’iI T0 TK1 TKC
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}U•” C-16 TIME TWI TWO TKI TKC
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TIME flit TC TKI TKO DPK DPW OPT V
- Page 206 and 207:
UN C5-18 TIME TWI TfD TKI TKO DPK C
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14.25 7.IC 10.2C 39.10 38.00 8.8 0.
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RUNJ C8-2C T[’E TWE T0 TKI (Hg) (
- Page 212 and 213:
TIVE M)*2 C) TWI TWO TKI TKC DPK op
- Page 214 and 215:
Tt’iE TWI TC TKI TKO OPK CPW DPT
- Page 216 and 217:
— A23 — APPENDIX 5 OALT2RATTUNS
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T—- TEI\iFERATUFE (°C) —I’ U
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d Average C Table A5.2 0.0452 0.025
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11.1 6.517 10.5 6.418 10.1 6.346 9.
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— A27 — Tib1e A6.2 Pun Dl .irn
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-A29- Table A6.4 Pun 1)3 ‘ Time (
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Time — A51 — Table A6.5 Run D5
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— A33 — APPENDIX 7 EOUNDARY LAY
- Page 232 and 233:
— ;55 — 1.7.3 Dimensionless Exp
- Page 234 and 235:
— = u — u = in — + ± + + or
- Page 236 and 237:
I A8.21 Data 2 Subroutines usng ite
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— ALf1 — Equations L.7.4.3 and
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— A1i•3 — Lt Prorran Use The
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DIM /\3.2./>. THE iJNI/E?j\I. \ELC)
- Page 244 and 245:
C DF1ENSIOH VIS(2.) REAL NUWSI INTE
- Page 246 and 247:
C C SUt3ROUTINE DATA INTEGER SR C C
- Page 248 and 249:
LI) I Li . 0 0 X .. (1•) U.. UI
- Page 250 and 251:
C C WRt 1E(6,’O) 60 FQR’AT(1HLf
- Page 252 and 253:
te 4Z’Xt’9’911’XZ’ 3DNVIS
- Page 254 and 255:
C C C C C )fl:O .0 DO ‘O 1=3,9,2
- Page 256 and 257:
C, .4:’. 0 0 —; —s iZ fl r;
- Page 258 and 259:
KINEMATIC VISCOSITY AT WALL 0.07407
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YP UP TP Y U T VIS TC CR PR 39.00 1