249 - 249 |
ISCRE 16 - Preface Burghardt A, Pohorecki R, Cybulski A |
251 - 267 |
Process intensification using multifunctional reactors Dautzenberg FM, Mukherjee M |
269 - 291 |
Continuous reactive chromatography Lode F, Houmard M, Migliorini C, Mazzotti M, Morbidelli M |
293 - 303 |
Microreaction engineering - is small better? Jensen KF |
305 - 322 |
Chemical reaction engineering aspects of fine chemicals manufacture Carpenter KJ |
323 - 332 |
Transport phenomena in polymeric membrane fuel cells Costamagna P |
333 - 341 |
Dynamics of the direct methanol fuel cell (DMFC): experiments and model-based analysis Sundmacher K, Schultz T, Zhou S, Scott K, Ginkel M, Gilles ED |
343 - 350 |
Reactive absorption: Optimal process design via optimal modelling Kenig EY, Schneider R, Gorak A |
351 - 357 |
A simplified procedure for the optimal design of autothermal reactors for endothermic high-temperature reactions Kolios G, Frauhammer J, Eigenberger G |
359 - 364 |
Process intensification in in-line monolithic reactor Stankiewicz A |
365 - 370 |
2-methylpropylacetate synthesis in a system of equilibrium reactor and reactive distillation column Smejkal Q, Hanika J, Kolena J |
371 - 379 |
Hydrodynamics in a ceramic pervaporation membrane reactor for resin production van der Gulik GJS, Janssen REG, Wijers JG, Keurentjes JTF |
381 - 386 |
Catalytic heat-exchanger reactor for strongly exothermic reactions Kirillov VA, Kuzin NA, Mescheryakov VD, Droboshevich VI |
387 - 394 |
Reactive distillation - industrial applications, process design & scale-up Tuchlenski A, Beckmann A, Reusch D, Dussel R, Weidlich U, Janowsky R |
395 - 402 |
Ethylene epoxidation in a catalytic packed-bed membrane reactor: experiments and model Al-Juaied MA, Lafarga D, Varma A |
403 - 410 |
A reactive distillation process for a cascade and azeotropic reaction system: Carbonylation of ethanol with dimethyl carbonate Luo HP, Xiao WD |
411 - 418 |
Design of a continuous process for the production of highly substituted granular carboxymethyl starch Tijsen CJ, Voncken RM, Beenackers AACM |
419 - 425 |
The dead core model applied to beads with immobilized cells in a fed-batch cephalosporin C production bioprocess Cruz AJG, Almeida RMRG, Araujo MLGC, Giordano RC, Hokka CO |
427 - 432 |
Chemo-enzymatic epoxidation of unsaturated plant oils Hilker I, Bothe D, Pruss J, Warnecke HJ |
433 - 442 |
Modeling of hydrogel immobilized enzyme reactors with mass-transport enhancement by electric field Pribyl M, Chmelikova R, Hasal P, Marek M |
443 - 452 |
Relation between flow pattern and de-activation of enzymes in stirred reactors Joshi JB, Sawant SB, Patwardhan AW, Patil DJ, Kshatriya SS, Nere NK |
453 - 458 |
Lactosucrose production using a simulated moving bed reactor Kawase M, Pilgrim A, Araki T, Hashimoto K |
459 - 466 |
Determination of sucrose effective diffusivity and intrinsic rate constant of hydrolysis catalysed by Ca-alginate entrapped cells Polakovic M, Kudlacova G, Stefuca V, Bales V |
467 - 474 |
The effect of pore-space morphology on the performance of anaerobic granular sludge particles containing entrapped gas Stepanek F, Marek M, Adler PM |
475 - 483 |
A biofilter network model - importance of the pore structure and other large-scale heterogeneities Schwarz BCE, Devinny JS, Tsotsis TT |
485 - 492 |
A networks-of-zones analysis of mixing and mass transfer in three industrial bioreactors Zahradnik J, Mann R, Fialova M, Vlaev D, Vlaev SD, Lossev V, Seichter P |
493 - 502 |
Development of a complete model for an air-lift reactor Camarasa E, Carvalho E, Meleiro LAC, Maciel R, Domingues A, Wild G, Poncin S, Midoux N, Bouillard J |
503 - 512 |
Eulerian simulations for determination of the axial dispersion of liquid and gas phases in bubble columns operating in the churn-turbulent regime van Baten JM, Krishna R |
513 - 522 |
Model evaluation for an industrial process of direct chlorination of ethylene in a bubble-column reactor with external recirculation loop Orejas JA |
523 - 529 |
Single- and two-phase flow in fixed-bed reactors: MRI flow visualisation and lattice-Boltzmann simulations Mantle MD, Sederman AJ, Gladden LF |
531 - 536 |
Gas-liquid mass transfer characteristics of the three-levels-of-porosity reactor van Hasselt BW, Calis HPA, Sie ST, van den Bleek CM |
537 - 545 |
Design and scale up of a bubble column slurry reactor for Fischer-Tropsch synthesis Krishna R, van Baten JM, Urseanu MI, Ellenberger J |
547 - 555 |
Experimental comparison of three reactor designs for photocatalytic water purification Dijkstra MFJ, Buwalda H, de Jong AWF, Michorius A, Winkelman JGM, Beenackers AACM |
557 - 564 |
Selective hydrogenation of 1,5,9-cyclododecatriene in up- and down-flow fixed-bed reactors: experimental observations and modeling Julcour C, Jaganathan R, Chaudhari RV, Wilhelm AM, Delmas H |
565 - 570 |
Neural network and hybrid model: a discussion about different modeling techniques to predict pulping degree with industrial data Aguiar HC, Maciel R |
571 - 578 |
Hydrodynamic modelling of dense gas-fluidised beds using the kinetic theory of granular flow: effect of coefficient of restitution on bed dynamics Goldschmidt MJV, Kuipers JAM, van Swaaij WPM |
579 - 585 |
Modelling radial dispersion in terms of the local structure of packed beds Schnitzlein K |
587 - 595 |
Determination of bed voidage using water substitution and 3D magnetic resonance imaging, bed density and pressure drop in packed-bed reactors Sharma S, Mantle MD, Gladden LF, Winterbottom JM |
597 - 603 |
Modelling and simulation of a steam reforming tube with furnace Grevskott S, Rusten T, Hillestad M, Edwin E, Olsvik O |
605 - 612 |
Heterogeneous reaction model for FCC riser units Martignoni W, de Lasa HI |
613 - 620 |
A pilot plant study and 2-D dispersion-reactor model for a high-density riser reactor Wei F, Wan XT, Hu YQ, Wang ZG, Yang YH, Jin Y |
621 - 626 |
Modelling and simulation of 1,2-dichloroethane production by ethylene oxychlorination in fluidized-bed reactor Al-Zahrani SM, Aljodai AM, Wagialla KM |
627 - 632 |
Design and simulation of a reactor for the chlorination of acetone in gaseous phase Markos J, Soos M, Jelemensky L |
633 - 639 |
Hydrogen production by catalytic cracking of methane over nickel gauze under periodic reactor operation Monnerat B, Kiwi-Minsker L, Renken A |
641 - 649 |
Heterogeneous reactor modeling for simulation of catalytic oxidation and steam reforming of methane Avci AK, Trimm DL, Onsan ZI |
651 - 658 |
Improving catalyst structures and reactor configurations for autothermal reaction systems: Application to solid oxide fuel cells Aguiar P, Lapena-Rey N, Chadwick D, Kershenbaum L |
659 - 666 |
Multilevel modelling of heterogeneous catalytic reactors Lakatos BG |
667 - 671 |
Modeling of hydrazodicarbonamide oxidation by chlorine in a gas-liquid-solid system Lin C, Zhang JY |
673 - 681 |
Simulation of a slurry airlift using a two-fluid model Oey RS, Mudde RF, Portela LM, van den Akker HEA |
683 - 692 |
Mechanistic investigation of electric field-activated self-propagating reactions: experimental and modeling studies Orru R, Cincotti A, Cao G, Munir ZA |
693 - 698 |
Liquid dispersion and holdup in a small-scale upflow hydrotreater at high temperatures and pressure Thanos AM, Galtier PA, Papayannakos NG |
699 - 705 |
Modelling of complex liquid-solid reaction systems in semibatch reactors: Claisen condensation in industrial scale Tirronen E, Salmi T, Lehtonen J, Vuori A, Gronfors O, Kaljula K |
707 - 711 |
The fractional Brownian motion as a model for an industrial airlift reactor Scheffer R, Maciel R |
713 - 719 |
Oxidative dehydrogenation of propane for propylene production -comparison of catalytic processes Wolf D, Dropka N, Smejkal Q, Buyevskaya O |
721 - 726 |
The modeling of a fountain photocatalytic reactor with a parabolic profile Li Puma G, Yue PL |