Table Of ContentChemical 
Engineering 
Journal 
Volume  88, issues  1—3,  28 September  2002 
www.elsevier.com/locate/cej 
Contents 
Abstracting Services 
This Journal is cited by the following Abstracting  Services:  BIOSEP Bulletin, BIOSIS, Cambridge  Scientific Abstracts, CABS, Chemical 
Abstracts, Chemical Engineering Abstracts, Current Contents, Engineered Materials Abstracts, Fluid Abstracts, FSTA, INSPEC, Material 
Business  Alerts,  Metals  Abstracts,  Mixing  and  Separation  Technology  Abstracts,  Pascal/CNRS,  Physikalische  Berichte,  Science 
Abstracts, Science Citation  Index, Theoretical Abstracts. 
General 
lsobaric vapour-—liquid  equilibrium of binary and ternary mixtures containing cyclohexane,  n-hexane, 1,3-dioxolane and 
1-butanol  at 40.0 and 101.3 kPa 
|. Gascon, S. Martin, H. Artigas, M.C. Lopez and C. Lafuente 
Column  hydraulics:  system limit/ultimate  capacity 
CW. Fitz Jr. and J.G. Kunesh 
Mixing pool model for prediction of distillation tray efficiency with liquid entrainment 
Z. Hongyan, W. Shuying, Z. Rongqi and D. Zhanting 
Viscosity estimation at low temperatures  (7, < 0.75) for organic liquids from group contributions 
H.-C.  Hsu, Y.-W. Sheu and C.-H. Tu 
Separation of zirconium and hafnium  using hollow fibers. Part |. Supported liquid membranes 
X.J. Yang, A.G. Fane and C. Pin 
Separation of zirconium and hafnium  using hollow fibres. Part Il. Membrane chromatography 
X.J. Yang, A.G. Fane and C. Pin 
Dissolution  kinetics of crystals in suspension and its application to L-aspartic acid crystals 
G. Shan, K. Igarashi and H. Ooshima 
Hydrodynamics and mass transfer in heterogeneous distillation with sieve tray column 
H.R. Mortaheb, H. Kosuge and K. Asano 
(contents continued on page !) 
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I 
1385 -8947( 20020928  )88:1-3;1-J
(contents continued from outside back cover) 
Study of the multicomponent system wet process phosphoric acid—methy|  isobutyl ketone at 40  °C phase equilibria and 
extraction  performances 
ee eens ee a kG  I  i  6  iad  big Wahl  he  he  le  Cake acy ove  sone  4.8 3146 caw  wend  Ob  eens  71 
Investigation of entropy effects during sorption of mixtures of alkanes in MFI zeolite 
Pe Perens ts  oo  wh.  ch  oe  bs  eee  oo  Os  Meals ote  ues  Kane  a  Ue  hi  ents é  oew  ee  wha  81 
Separation of phenol from aqueous solutions by polymeric reversed  micelle extraction 
peek  eR  ae ee  RE  a  a  er  ee  ne  ee  95 
Quality of borage seed oil extracted  by liquid and supercritical carbon dioxide 
aren  ann I nt, UU  hnsi, he ob bie ita Waa h atha s oda ele dwaleons  103 
Measurement of gas hold-up in bubble columns from low frequency acoustic emissions 
es  CI  os  ods  x04  CS  Red  FS  CERT  be  FEA  0  0o  6  ew  EC  RETNA  COT  has  Cbd  CROC  o  use  eee  eR:  111 
Mass transfer from solid particles to power law non-Newtonian  fluid in granular bed at low Reynolds numbers 
ee Oe, Se  sg  |  sy  aise beac eaaed +  eee  aes  as  6s  BEBE  A  eee  aes  Eek  ohdees  119 
Interdrop coalescence with mass transfer:  comparison of the approximate drainage models with numerical  results 
A. Gabon, S. Alemenarove, C, Gurr  Gre FAK. CTOORTS  nna  coc  cc  ccc  weapawee  bab  ecctbvasecceoscsccee  127 
Radial solids flow structure in a liquid—solids circulating fluidized bed 
ey es Ok, Gey Gs HE ET PL CI sae  000  a  hd  ne  Wk  ea)  640  6  0'ee 2eb  ts  eUbh  oe  os  hegieeeelareess  141 
Characterizing  particle aggregates in a high-density and high-flux CFB riser 
RE  ee  ee  Pee  ee] eee eT ee  eee  errr ee ne  151 
Application of model  predictive control and dynamic analysis to a pilot distillation column and experimental verification 
ee Pe ae See: Os SY I  No  6b  a  Vice  ae  wee  Oe  beet  e  eee  al  weet  pa  seasepek  cs  eeies  163 
Effect of feed on optimal thermodynamic performance of a distillation column 
ee  i  nnd  ein 6  Oo  RRA  Wee  Ab  Oe  eee  Ce  Ub  eb  cick s  ood  see)  6en  bee  bes  4s  ees  oie  es  kaos 
Chemical  Reaction  Engineering 
Incorporating  zeolites in microchemical  systems 
es  s,s  ss  va  40h  &  00  wee  nw  bee.  cle eb  oe  kek  eer  ebe  cae  eee  eee  187 
Phase transitions in the active component of vanadium  catalyst for sulfur dioxide oxidation:  crystal phase dissolving 
PEP: STV, SL PROUT GN TG, TOTTI  6  nc  ccc  ccc  crest  ibereecetewervacscwettevenssuns  201 
Local overall gas—liquid  mass transfer coefficient in  a gas—liquid—solid  reversed flow jet loop reactor 
ey  2  he  Bia  Rae  bie  Celi  ae  &  Ob  G  b.na 06  Jae  pees  Od  Owls whee  209 
Catalytic decomposition  process of cumene  hydroperoxide using sulfonic resins as catalyst 
ee  De  aN  ae a  Sh  hlaca hd  pao  SW, ware bd  WG  Ales OCR  RE  Re  Oe  ARS  ERED  eSO s  MWelee  215 
Comparative study of two chemical  reactions with different behaviour in batch and semibatch  reactors 
ee  ee  as.  5  6  0  ooo  5  6  0  0:6e 0  bb  waa  Che  Rae  on  SS  6  oe  wale S  Os  When  bis b's  bebe  225 
Pressure drop and flow regimes in cocurrent gas-liquid upflow through packed beds 
rN  Oy he  hn  2s  5  XL  da 'ans' 65  SGA  SO  ah  oie bo  Es  5:0 46  a  Daas  0  44  ba  oe  CURE  ORDO  233 
Comment on “Pressure drop and flow regime in cocurrent gas-liquid upflow through packed beds”  [Chem. Eng. J. 88 
(2002) 233-243] 
A  NE  eae  an  oid  CW  dew a  he  Saad  We  Ub'n Sede  e  6+  ek  OPENER ECO  eee  245 
Reply for the comments  on “Pressure drop and flow regime in cocurrent gas—liquid upflow through packed beds” 
[Chem. Eng. J. 88 (2002) 233-243] 
UY  Oe I  3  DS  o's 5  b  0'k bine  eed  050.0 CR  Wes  Sh  cain  POSS  SRR  SS  FO  eieR CRE  R*  ee  eme 
Environmental  Chemical  Engineering 
Formation  process of mixed fouling of microbe and CaCO, in water systems 
ee ae ee  Rs  Be  re  sls  ak)  &  Gale  OW  ae  eka. cce's 666k  Me  eed  che  o0-00 80  eed  eee  tee  ORs  249 
Evaluation of the thermodynamic  parameters for the adsorption of some hydrocarbons on 4A and 13X zeolites by 
inverse gas chromatography 
ee ee Se, A A  os  aie dain cha  Ce  oule  5  MRSS  CRON  UD  Cdk  wpe  ees  ciged Cewesseeey  255 
I  aeSe at el ae ee   I  ee  ng edhe eer 
a  as  a  eeea hs abe koa aieda a bd bead od ba Sane 6 Caeees 
IE  oe eee. OO  ra  eee ren  ae  re. +)  a  ry  Pela  ne pee te  oe  Yee  eee  eee