1927 - 1927 |
Chemical Reaction Engineering for the 21st century - Part A -Newport Beach, California - 13-16 September 1948 - Preface Gavalas GR, Tsotsis TT |
1929 - 1939 |
Computational chemistry and process design Dixon DA, Feller D |
1941 - 1957 |
Chemical reaction engineering in the design of CVD reactors Komiyama H, Shimogaki Y, Egashira Y |
1959 - 1973 |
Environmentally friendly processes Pereira CJ |
1975 - 1995 |
Multiphase reactors - revisited Dudukovic MP, Larachi F, Mills PL |
1997 - 2017 |
High-temperature membrane reactors: potential and problems Saracco G, Neomagus HWJP, Versteeg GF, van Swaaij WPM |
2019 - 2027 |
Modeling the hydrodynamics of downer reactors based on kinetic theory Cheng Y, Guo YC, Wei F, Jin Y, Lin WY |
2029 - 2037 |
Natural gas combustion in a turbulent fluidized bed of inert particles Sotudeh-Gharebaagh R, Chaouki J, Legros R |
2039 - 2045 |
Two-phase model for a catalytic turbulent fluidized-bed reactor: Application to ethylene synthesis Chaouki J, Gonzalez A, Guy C, Klvana D |
2047 - 2054 |
Gamma radiation densitometry for studying the dynamics of fluidized beds Mudde RF, Harteveld WK, van den Akker HEA, van der Hagen THJJ, van Dam H |
2055 - 2065 |
An experimental and numerical study of turbulent swirling flow in gas cyclones Hoekstra AJ, Derksen JJ, Van Den Akker HEA |
2067 - 2075 |
Studies on gas-solid-solid circulating fluidized-bed reactors Huang SY, Wang ZW, Jin Y |
2077 - 2083 |
Particle-motion-resolved discrete model for simulating gas-solid fluidization Ouyang J, Li JH |
2085 - 2093 |
CFD modeling of an internally circulating fluidized-bed reactor Marschall KJ, Mleczko L |
2095 - 2102 |
Fluidized-bed steam methane reforming with oxygen input Roy S, Pruden BB, Adris AM, Grace JR, Lim CJ |
2103 - 2112 |
Scale-up of bottom-bed dynamics and axial solids-distribution in circulating fluidized beds of Geldart-B particles Schouten JC, Zijerveld RC, van den Bleek CM |
2113 - 2122 |
Dynamics of fluidized-bed reactors. Development and application of a new multi-fiber optical probe Tayebi D, Svendsen HF, Grislingas A, Mejdell T, Johannessen K |
2123 - 2130 |
Development of a downer reactor for fluid catalytic cracking Talman JA, Geier R, Reh L |
2131 - 2139 |
The development of a dual fluidized-bed reactor system for the conversion of hydrogen chloride to chlorine Mortensen M, Minet RG, Tsotsis TT, Benson SW |
2141 - 2149 |
Validation of the Eulerian simulated dynamic behaviour of gas-solid fluidised beds van Wachem BGM, Schouten JC, Krishna R, van den Bleek CM |
2151 - 2160 |
Mixing and reaction in the circulating fluidized bed - A three-dimensional combustor model Knoebig T, Luecke K, Werther J |
2161 - 2173 |
Axial flow structure in the entrance region of a downer fluidized bed: Effects of the distributor design Johnston PM, de Lasa HI, Zhu JX |
2175 - 2185 |
A generalized bubbling turbulent fluidized-bed reactor model Thompson ML, Bi HT, Grace JR |
2187 - 2197 |
Fluid dynamic parameters in bubble columns with internals Chen JW, Li F, Degaleesan S, Gupta P, Al-Dahhan MH, Dudukovic MP, Toseland BA |
2199 - 2207 |
Comparative hydrodynamics study in a bubble column using computer-automated radioactive particle tracking (CARPT)/computed tomography (CT) and particle image velocimetry (PIV) Chen JW, Kemoun A, Al-Dahhan MH, Dudukovic MP, Lee DJ, Fan LS |
2209 - 2216 |
Continuous flow bubble column reactor for the photocatalytic causticisation of sodium oxalate Lea J, Adesina AA |
2217 - 2226 |
A three-dimensional CFD model for gas-liquid bubble columns Delnoij E, Kuipers JAM, van Swaaij WPM |
2227 - 2236 |
Gas disengagement technique in a slurry bubble column operated in the coalesced bubble regime Lee DJ, Luo X, Fan LS |
2237 - 2246 |
Gas holdup and mass transfer in bubble column reactors operated at elevated pressure Letzel HM, Schouten JC, Krishna R, van den Bleek CM |
2247 - 2254 |
Bubbles in non-Newtonian fluids: Formation, interactions and coalescence Li HAZ |
2255 - 2262 |
Hydrodynamics and mass transfer in an airlift reactor Korpijarvi J, Oinas P, Reunanen J |
2263 - 2271 |
Hydrodynamics of gas-lift reactors with a fast, liquid-phase reaction Marquez MA, Amend RJ, Carbonell RG, Saez AE, Roberts GW |
2273 - 2284 |
Applicability of the standard k-epsilon turbulence model to the dynamic simulation of bubble columns: Part I. Detailed numerical simulations Sokolichin A, Eigenberger G |
2285 - 2293 |
CFD modelling and mixing in stirred tanks Sahu AK, Kumar P, Patwardhan AW, Joshi JB |
2295 - 2303 |
Impact of an undesired reaction on a boiling slurry reactor Khinast J, Luss D, Leib TM, Harold MP |
2305 - 2315 |
Gas-liquid flow in stirred reactors: Trailing vortices and gas accumulation behind impeller blades Ranade VV, Deshpande VR |
2317 - 2323 |
Behavior of fine particles in the vicinity of a gas bubble in a stagnant and a moving fluid Roizard C, Poncin S, Lapicque F, Py X, Midoux N |
2325 - 2337 |
Experimental study of the effect of bubbles, drops and particles on the product distribution for a mixing sensitive, parallel-consecutive reaction system Brilman DWF, Antink R, van Swaaij WPM, Versteeg GF |
2339 - 2349 |
On the role of micro- and mesomixing in a continuous Couette-type precipitator Barresi AA, Marchisio D, Baldi G |
2351 - 2358 |
Monolithic reactors for fine chemicals industries: A comparative analysis of a monolithic reactor and a mechanically agitated slurry reactor Cybulski A, Stankiewicz A, Albers RKE, Moulijn JA |
2359 - 2370 |
A fluid dynamic model for three-phase airlift reactors Garcia-Calvo E, Rodriguez A, Prados A, Klein J |
2371 - 2379 |
Cold flow studies and computer simulation of a slurry transport reactor for the alkylation of isobutane using zeolite-based catalysts Ketikidis PT, Spourtoudi CG, Ttjatjopoulos GJ, Vasalos IA |
2381 - 2389 |
Hydrodynamics and mass transfer issues in a countercurrent gas-liquid internally finned monolith reactor Lebens PJM, Stork MM, Kapteijn F, Sie ST, Moulijn JA |
2391 - 2400 |
Dynamics of a three-phase upflow fixed-bed catalytic reactor Julcour C, Stuber F, Le Lann JM, Wilhelm AM, Delmas H |
2401 - 2408 |
The effect of surface active additives on bubble coalescence and gas holdup in viscous aerated batches Zahradnik J, Kuncova G, Fialova M |
2409 - 2419 |
Two-phase flow distribution in 2D trickle-bed reactors Jiang Y, Khadilkar MR, Al-Dahhan MH, Dudukovic MP |
2421 - 2431 |
Trickle-bed reactor models for systems with a volatile liquid phase Khadilkar MR, Mills PL, Dudukovic MP |
2433 - 2439 |
Computational fluid dynamics simulations of fluid flow and heat transfer at the wall-particle contact points in a fixed-bed reactor Logtenberg SA, Nijemeisland M, Dixon AG |
2441 - 2452 |
A single events kinetic model for the hydrocracking of paraffins in a three-phase reactor Schweitzer JM, Galtier P, Schweich D |
2453 - 2458 |
Optimal product distribution from laminar flow reactors: Newtonian and other power-law fluids Levien KL, Levenspiel O |
2459 - 2466 |
Modelling of industrial S-PVC reactor Mejdell T, Pettersen T, Naustdal C, Svendsen HF |
2467 - 2473 |
Hybrid first-principle-neural-network approach to modelling of the liquid-liquid reacting system Molga E, Cherbanski R |
2475 - 2480 |
Analysis of simulated moving-bed reactors Migliorini C, Fillinger M, Mazzotti M, Morbidelli M |
2481 - 2489 |
Dynamic simulation of bubbly flow in bubble columns Pan Y, Dudukovic MP, Chang M |
2491 - 2500 |
Three-dimensional numerical simulation of flow and heat transfer in the Sulzer SMX static mixer Visser JE, Rozendal PF, Hoogstraten HW, Beenackers AACM |
2501 - 2511 |
Application of the Maxwell-Stefan theory to the transport in ion-selective membranes used in the chloralkali electrolysis process van der Stegen JHG, van der Veen AJ, Weerdenburg H, Hogendoorn JA, Versteeg GF |
2513 - 2519 |
A concept to simulate an industrial size tube reactor with fast complex kinetics and absorption of two gases on the basis of CFD modeling Warnecke HJ, Schafer M, Pruss J, Weidenbach M |
2521 - 2526 |
A hybrid neural network-first principles model for fixed-bed reactor Qi HY, Zhou XG, Liu LH, Yuan WK |
2527 - 2533 |
Modeling of heat transfer in wall-cooled tubular reactors Koning GW, Westerterp KR |
2535 - 2543 |
Recent results in optimal reactor synthesis via attainable region theory Feinberg M |
2545 - 2554 |
Solids dynamics from experimental trajectory time-series of a single particle motion in gas-spouted beds Cassanello M, Larachi F, Legros R, Chaouki J |
2555 - 2559 |
Mathematical modelling of self-sustained isothermal oscillations in N2O decomposition on Cu-ZSM5 Ciambelli P, Di Benedetto A, Pirone R, Russo G |
2561 - 2568 |
Hydrogenation of crotonaldehyde under periodic flow interruption in a trickle bed Stradiotto DA, Hudgins RR, Silveston PL |
2569 - 2573 |
Forced periodic operation of a trickle-bed reactor Lange R, Gutsche R, Hanika J |
2575 - 2583 |
Forced composition cycling of a novel thermally self-sustaining fluidised-bed reactor for methane reforming Opoku-Gyamfi K, Adesina AA |
2585 - 2595 |
Parametric study of unsteady-state flow modulation in trickle-bed reactors Khadilkar MR, Al-Dahhan MH, Dudukovic MP |
2597 - 2607 |
Coupled reaction zones in a circulation loop reactor Mangold M, Kienle A, Gilles ED, Richter M, Roschka E |
2609 - 2618 |
Nonstationary operation of a system of catalytic monolithic reactors for selective NOx reduction Jirat J, Stepanek F, Kubicek M, Marek M |
2619 - 2626 |
Periodic operation of the Deacon process Nieken U, Watzenberger O |
2627 - 2635 |
Investigation of spatially patterned catalytic reactors Cote AS, Delgass WN, Ramkrishna D |
2637 - 2646 |
Styrene synthesis in a reverse-flow reactor Kolios G, Eigenberger G |
2647 - 2657 |
Design of periodic adsorptive reactors for the optimal integration of reaction, separation and heat exchange Yongsunthon I, Alpay E |
2659 - 2667 |
A simplified model for management of resonance exotherms in fixed-bed reactors using liquid carriers Korre SC, Wyatt JT, Dankworth DC, Koros RM |
2669 - 2678 |
Nonlinear control of spatially inhomogenous aerosol processes Kalani A, Christofides PD |
2679 - 2688 |
Reaction profile control of the continuous pulp digester Doyle FJ, Kayihan F |
2689 - 2696 |
Implementation of observer for on-line estimation of concentration in continuous-stirred membrane bioreactor: Application to the fermentation of lactose Lombardi M, Fiaty K, Laurent P |
2697 - 2706 |
Dynamic simulation and optimization of a catalytic steam reformer Kvamsdal HM, Svendsen HF, Hertzberg T, Olsvik O |
2707 - 2714 |
Methodology of dynamic optimization and optimal control of batch electrochemical reactors Fournier F, Latifi MA, Valentin G |
2715 - 2720 |
Optimal changeover profiles for an industrial depropanizer Fikar M, Latifi MA, Creff Y |
2721 - 2729 |
Synthesis of reactive and combined reactor separation systems utilizing a mass heat exchange transfer module Ismail SR, Pistikopoulos EN, Papalexandri KP |
2731 - 2738 |
Application of fuzzy causal networks to waste water treatment plants Huang YC, Wang XZ |
2739 - 2744 |
Optimizing control of a wall-cooled fixed-bed reactor Zhou XG, Liu LH, Yan WK |
2745 - 2751 |
Production optimization with operating constraints for a fed-batch reactor with DMC predictive control Rodrigues JAD, Marciel R |
2753 - 2764 |
Future directions in modelling the FCC process: An emphasis on product quality Christensen G, Apelian MR, Hickey KJ, Jaffe SB |
2765 - 2772 |
Optimisation of the process conditions for the modification of starch Tijsen CJ, Scherpenkate HJ, Stamhuis EJ, Beenackers AACM |
2773 - 2779 |
Production of high quality gasoline from waste polyethylene derived heavy oil over Ni-REY catalyst in steam atmosphere Masuda T, Kuwahara H, Mukai SR, Hashimoto K |
2781 - 2785 |
The effect of dilution on the liquid-phase non-idealities in pilot scale upflow reactors Thanos AM, Galtier PA, Papayannakos NG |
2787 - 2792 |
Kinetic understanding of the chemical synergy under LPDME (TM) conditions - once-through applications Peng XD, Toseland BA, Tijm PJA |
2793 - 2798 |
Modelling and scale-up of a loop reactor for hydrogenation processes Lehtonen J, Kaplin J, Salmi T, Haario H, Vuori A, Tirronen E |
2799 - 2806 |
Kinetic and catalytic aspects in the hydrogen peroxide production via anthraquinone Santacesaria E, Di Serio M, Russo A, Leone U, Velotti R |
2807 - 2815 |
Zeolite membrane reactor for isobutane dehydrogenation: Experimental results and theoretical modelling Casanave D, Ciavarella P, Fiaty K, Dalmon JA |
2817 - 2827 |
Rigorous model and experimental verification of the radiation field in a flat-plate solar collector simulator employed for photocatalytic reactions Brandi RJ, Alfano OM, Cassano AE |
2829 - 2838 |
The radially vibrating horn: A scaling-up possibility for sonochemical reactions Dahlem O, Reisse J, Halloin V |
2839 - 2847 |
Multiple reactions in catalytic distillation processes for the production of the fuel oxygenates MTBE and TAME: Analysis by rigorous model and experimental validation Sundmacher K, Uhde G, Hoffmann U |
2849 - 2858 |
Activated solid-fluid reactions in ultrasound reactors Horst C, Kunz U, Rosenplanter A, Hoffmann U |
2859 - 2864 |
Acceleration of chemical reaction by AOT micelles under supercritical conditions Ikushima Y, Shervani Z, Saito R, Hatakeda K, Sato O, Aizawa T, Arai M |
2865 - 2872 |
Modeling of linear pressure fields in sonochemical reactors considering an inhomogeneous density distribution of cavitation bubbles Dahnke SW, Keil FJ |
2873 - 2881 |
The influence of mass transfer and mixing on the performance of a tray column for reactive distillation Higler AP, Taylor R, Krishna R |
2883 - 2888 |
Micromixing effects in a couette flow reactor Liu CI, Lee DJ |
2889 - 2898 |
Reversed flow converter for emission control after automotive engines Matros YS, Bunimovich GA, Strots VO, Mirosh EA |
2899 - 2905 |
A predictive CFD model for a falling particle receiver reactor exposed to concentrated sunlight Meier A |
2907 - 2916 |
Modeling and experimentation of molten carbonate fuel cell reactors in a scale-up process Bosio B, Costamagna P, Parodi F |
2917 - 2925 |
Simulation of an inert membrane reactor for the oxidative dehydrogenation of butane Tellez C, Menendez M, Santamaria J |
2927 - 2936 |
Direct methanol polymer electrolyte fuel cell: Analysis of charge and mass transfer in the vapour-liquid-solid system Sundmacher K, Scott K |
2937 - 2945 |
Design and operation of a membrane reactor for electrochemical gas purification Sundmacher K, Hoffmann U |
2947 - 2951 |
Microchannel reactors for fuel processing applications. I. Water gas shift reactor Tonkovich AY, Zilka JL, LaMont MJ, Wang Y, Wegeng RS |
2953 - 2961 |
The influence of ultrasound on micromixing in a semi-batch reactor Monnier H, Wilhelm AM, Delmas H |
2963 - 2967 |
Mass transfer in gas-liquid Couette-Taylor flow in membrane reactor Wronski S, Dluska E, Hubacz R, Molga E |
2969 - 2977 |
Studies on paired packed-bed electrode reactor: Modeling and experiments Zhang XS, Wu GB, Ding P, Zhou XG, Yuan WK |
2979 - 2984 |
Conversion targets for plug flow membrane reactors Chmielewski D, Ziaka Z, Manousiouthakis Y |
2985 - 2990 |
Solid-solid reaction with mechanical coupling Viljoen HJ, Hlavacek V |