Table Of Content

Chemical 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 !) SCIENCE Full text of this journal is available, on-line from ScienceDirect. Visit www.sciencedirect.com for more information. The publisher encourages the submission of articles in electronic form thus saving time and avoiding rekeying errors. A leaflet describing our requirements is available from the publisher upon request CONTE NTS This journal is part of ContentsDirect, the free alerting service which sends tables of contents by e-mail for Elsevier Science books and journals. You can register for 6 ContentsDirect online at: www.elsevier.com/locate/contentsdirect 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