727 - 734 |
Effect of ion excess on particle size and morphology during barium sulphate precipitation: an experimental study Wong DCY, Jaworski Z, Nienow AW |
735 - 739 |
Droplet size distribution in a continuous oscillatory baffled reactor Pereira NE, Ni XW |
741 - 746 |
Scale-up effects on the drop size distribution of liquid-liquid dispersions in agitated vessels Podgorska W, Baldyga J |
747 - 754 |
Liquid flow velocity measurements in stirred tanks by ultra-sound Doppler velocimetry Bouillard J, Alban B, Jacques P, Xuereb C |
755 - 761 |
Distribution of suspended particles in a Taylor-Poiseuille vortex flow reactor Resende MM, Tardioli PW, Fernandez VM, Ferreira ALO, Giordano RLC, Giordano RC |
763 - 769 |
Macro-mixing, partial segregation and 3-D selectivity fields inside a semi-batch stirred reactor Rahimi M, Mann R |
771 - 778 |
Spatiotemporal patterns in models of cross-flow reactors. Regular and oscillatory kinetics Nekhamkina O, Rubinstein BY, Sheintuch M |
779 - 787 |
Oxidative dehydrogenation of light paraffins in novel short contact time reactors. Experimental and theoretical investigation Beretta A, Ranzi E, Forzatti P |
789 - 798 |
A Monte Carlo model for the sintering of Ni/Al2O3 catalysts Teixeira ACSC, Giudici R |
799 - 804 |
Key factors for the encapsulation of Keggin-type heteropoly acids in the supercages of Y-type zeolite Mukai SR, Lin L, Masuda T, Hashimoto K |
805 - 812 |
Hydrodynamic aspects of the monolith loop reactor Heiszwolf JJ, Engelvaart LB, van den Eijnden MG, Kreutzer MT, Kapteijn F, Moulijn JA |
813 - 821 |
Radial and axial dispersion of the liquid phase within a KATAPAK-S (R) structure: experiments vs. CFD simulations van Baten JM, Ellenberger J, Krishna R |
823 - 829 |
Monolithic catalysts as efficient three-phase reactors Nijhuis TA, Kreutzer MT, Romijn ACJ, Kapteijn F, Moulijn JA |
831 - 839 |
High-temperature combustion of CH4 over PdO/Al2O3: kinetic measurements in a structured annular reactor Groppi G, Ibashi W, Valentini M, Forzatti P |
841 - 847 |
The polylith reactor as an alternative to the monolith and the randomly packed-bed reactor IJselendoorn HC, Calis HPA, van den Bleek CM |
849 - 857 |
Selective catalytic reduction of NOx over zeolite-coated structured catalyst packings Seijger GBF, Oudshoorn OL, Boekhorst A, van Bekkum H, van den Bleek CM, Calis HPA |
859 - 864 |
Modelling of Katapak reactor for hydrogenation of anthraquinones Piironen M, Haario H, Turunen I |
865 - 872 |
Coke burnoff in a typical FCC particle analyzed by an SEM mapped 2-D network pore structure El-Nafaty UA, Mann R |
873 - 879 |
Residual thermodynamic properties in reactor modeling Prior JMV, Loureiro JM |
881 - 888 |
Development and characterization of Pt-SnO2/gamma-Al2O3 catalysts Akin AN, Kilaz G, Isli AI, Onsan ZI |
889 - 896 |
Effective diffusivities of lighter hydrocarbons in Cu- and Co-MFI-type zeolite catalysts Masuda T, Okubo Y, Mukai SR, Kawase M, Hashimoto K, Shichi A, Satsuma A, Hattori T, Kiyozumi Y |
897 - 904 |
Recovery of useful hydrocarbons from oil palm waste using ZrO2 supporting FeOOH catalyst Masuda T, Kondo Y, Miwa M, Shimotori T, Mukai SR, Hashimoto K, Takano M, Kawasaki S, Yoshida S |
905 - 910 |
A continuum approach for the active sites in a Ziegler-Natta catalytic system Ha KS, Rhee HK |
911 - 915 |
Reducing the gel effect in free radical polymerization Cioffi M, Hoffmann AC, Janssen LPBM |
917 - 925 |
Recent developments in the particle size distribution modeling of fluidized-bed olefin polymerization reactors Yiannoulakis H, Yiagopoulos A, Kiparissides C |
927 - 935 |
Experimental and modeling studies of oligomerization and copolymerization of dicyclopentadiene Palmova I, Kosek J, Schongut J, Marek M, Stepanek K |
937 - 943 |
Role of active chain segregation in emulsion polymerization Ghielmi A, Storti G, Morbidelli M |
945 - 953 |
Micro-kinetics and mass transfer in poly(ethylene terephthalate) synthesis Rieckmann T, Volker S |
955 - 962 |
Production of copolymers with a predefined intermolecular chemical composition distribution by emulsion polymerisation in a continuously operated reactor Scholtens CA, Meuldijk J, Drinkenburg AAH |
963 - 969 |
Heterogeneous modeling for fluidized-bed polymerization reactor Fernandes FAN, Lona LMF |
971 - 979 |
Detailed mechanistic modeling of polymer degradation: application to polystyrene Kruse TM, Woo OS, Broadbelt LJ |
981 - 988 |
Wavelet analysis of dynamic behavior in fluidized beds Ren JQ, Mao QM, Li JH, Lin WG |
989 - 997 |
Dynamic optimization and production planning of thermal cracking operation Edwin EH, Balchen JG |
999 - 1010 |
Multi-objective optimization of industrial hydrogen plants Rajesh JK, Gupta SK, Rangaiah GP, Ray AK |
1011 - 1019 |
Spatially patterned catalytic reactors. Feasibility issues Cote AS, Delgass WN, Ramkrishna D |
1021 - 1028 |
Optimization of a cocktail of initiators for suspension polymerization of vinyl chloride in batch reactors Pinto JM, Giudici R |
1029 - 1033 |
Microreactors, a new efficient tool for optimum reactor design Worz O, Jackel KP, Richter T, Wolf A |
1035 - 1039 |
Optimization of a continuous pulsed corona reactor Srinivasan B, Palanki S, Grymonpre DR, Locke BR |
1041 - 1047 |
A unified correlation for predicting liquid axial dispersion coefficient in bubble columns Moustiri S, Hebrard G, Thakre SS, Roustan M |
1049 - 1056 |
Phase distribution phenomena in two-phase bubble column reactors Jakobsen HA |
1057 - 1065 |
Predictions of flow transitions in a bubble column by chaotic time series analysis of pressure fluctuation signals Lin TJ, Juang RC, Chen YC, Chen CC |
1067 - 1074 |
Multiscale modeling of hydrodynamics, mass transfer and reaction in bubble column reactors Bauer M, Eigenberger G |
1075 - 1083 |
Gas absorption in an agitated gas-liquid-liquid system Cents AHG, Brilman DWF, Versteeg GF |
1085 - 1093 |
Influence of gas distribution and regime transitions on liquid velocity and turbulence in a 3-D bubble column Vial C, Laine R, Poncin S, Midoux N, Wild G |
1095 - 1101 |
Absorption of sulfur dioxide into aqueous reactive slurries of calcium and magnesium hydroxide in a stirred cell Dagaonkar MV, Beenackers AACM, Pangarkar VG |
1103 - 1110 |
Local gas hold-up measurements in fluidized bed and slurry bubble column Schweitzer JH, Bayle J, Gauthier T |
1111 - 1116 |
Hydrodynamics of a co-current three-phase solid-bed reactor for foaming systems Szlemp A, Janecki D, Bartelmus G |
1117 - 1125 |
Comparison of single- and two-bubble class gas-liquid recirculation models - application to pilot-plant radioactive tracer studies during methanol synthesis Gupta P, Al-Dahhan MH, Dudukovic MP, Toseland BA |
1127 - 1130 |
Prediction of axial liquid velocity profile in bubble columns Wu YX, Al-Dahhan MH |
1131 - 1136 |
Mass transfer in gas-liquid Couette-Taylor flow reactor Dluska E, Wronski S, Hubacz R |
1137 - 1141 |
Flow of non-Newtonian fluids around bubbles: PIV measurements and birefringence visualisation Funfschilling D, Li HZ |
1143 - 1149 |
Effects of macroscopic hydrodynamics on heat transfer in bubble columns Lin TJ, Wang SP |
1151 - 1157 |
Performance of confined plunging liquid jet bubble column as a gas-liquid reactor Evans GM, Bin AK, Machniewskj PM |
1159 - 1166 |
A transport equation for the interfacial area density applied to bubble columns Lehr F, Mewes D |
1167 - 1174 |
Hydrodynamics of a pilot plant bubble column under elevated temperature and pressure Pohorecki R, Moniuk W, Zdrojkowski A, Bielski P |
1175 - 1180 |
Hydrocarbon selectivity model for the slurry phase Fischer-Tropsch synthesis on precipitated iron catalysts Nowicki L, Ledakowicz S, Bukur DB |
1181 - 1187 |
Particle-liquid heat transfer in trickle-bed reactors Boelhouwer JG, Piepers HW, Drinkenburg AAH |
1189 - 1195 |
Hydrodynamic behavior of a trickle bed reactor under "forced" pulsing flow Xiao Q, Cheng ZM, Jiang ZX, Anter AM, Yuan WK |
1197 - 1205 |
Gas holdup in a trayed cold-flow bubble column Kemoun A, Rados N, Li F, Al-Dahhan MH, Dudukovic MP, Mills PL, Leib TM, Lerou JJ |
1207 - 1210 |
Predictions of radial gas holdup profiles in bubble column reactors Wu YX, Ong BC, Al-Dahhan MH |