4293 - 4293 |
Proceedings of the Third International Conference on Unsteady State Processes in Catalysis, St Petersburg, Russia, 28 June-3 July 1998 - Preface Bunimovich GA |
4295 - 4304 |
Monte-Carlo methods for simulating the catalytic oxidative dehydrogenation of propane over VMgO catalyst Boudeville Y, Kolb M, Pantazidis A, Marquez-Alvarez C, Mirodatos C, Elokhin V |
4305 - 4314 |
Unsteady-state studies of oxidation and hydrogenation catalytic processes Kiperman SL, Gaidai NA, Nekrasov NV, Botavina MA, Duisenbaev SE |
4315 - 4325 |
Oxidative dehydrogenation of propane on V2O5/TiO2 catalysts under transient conditions Genser F, Pietrzyk S |
4327 - 4335 |
On the oxygen effect in nitric oxide reduction by methane over Co/ZSM-5 Pinaeva LG, Sadovskaya EM, Suknev AP, Goncharov VB, Sadykov VA, Balzhinimaev BS, Decamp T, Mirodatos C |
4337 - 4342 |
Unsteady processes and aerosol catalysis Glikin M, Kutakova D, Prin E |
4343 - 4349 |
Investigation of the catalytic decomposition of NO and N2O on supported Rh with transient techniques Rahkamaa K, Salmi T |
4351 - 4357 |
Study of thermocatalytic decomposition of polyethylene and polyvinyl alcohol in the presence of an unsteady-state Fe-containing catalyst Maksimova NI, Krivoruchko OP |
4359 - 4364 |
Kinetic investigation and mathematical modeling of oscillation regimes for oxidative dehydrogenation of butene-1 Tomilov VN, Zagoruiko AN, Kuznetsov PA |
4365 - 4370 |
Oxygen partial pressure effects on the oxidative dehydrogenation of propane Creaser D, Andersson B, Hudgins RR, Silveston PL |
4371 - 4378 |
Thin-zone TAP-reactor - theory and application Shekhtman SO, Yablonsky GS, Chen S, Gleaves JT |
4379 - 4384 |
Application of the TAP-2 reactor and FTIR in elucidating the mechanism of NO2 reduction by propene over an acidic mordenite Gerlach T, Baerns M |
4385 - 4395 |
The conversion of methanol to olefins: a transient kinetic study Dewaele O, Geers VL, Froment GF, Marin GB |
4397 - 4405 |
Selective and non-selective oxygen species determining the product selectivity in the oxidative conversion of propane over vanadium mixed oxide catalysts Zanthoff HW, Buchholz SA, Pantazidis A, Mirodatos C |
4407 - 4421 |
Propane ammoxidation on an Al-Sb-V-W-oxide catalyst. A mechanistic study using the TAP-2 reactor system Hinz A, Andersson A |
4423 - 4436 |
Measurement and modeling of the transient adsorption, desorption and diffusion processes in microporous materials Nijhuis TA, van den Broeke LJP, Linders MJG, van de Graaf JM, Kapteijn F, Makkee M, Moulijn JA |
4437 - 4448 |
Cyclic operation of the oxidative dehydrogenation of propane Creaser D, Andersson B, Hudgins RR, Silveston PL |
4449 - 4457 |
Effect of diffusion and adsorption-desorption on periodic operation performance of NO-CO reaction over supported noble metal catalysts Aida T, Na-Ranong D, Kobayashi R, Niiyama H |
4459 - 4468 |
CO oxidation in a fixed bed reactor with high frequency cycling of the feed Hoebink JHBJ, Nievergeld AJL, Marin GB |
4469 - 4474 |
Reactor performance enhancement under periodic operation for the ethanol dehydration over gamma-alumina, a reaction with a stop-effect Golay S, Doepper R, Renken A |
4475 - 4482 |
SO2 oxidation method. Mathematical modeling taking into account dynamic properties of the catalyst Vernikovskaya NV, Zagoruiko AN, Noskov AS |
4483 - 4499 |
The feedback mechanism in self-oscillations for CO oxidation over EUROPT-3 van Neer F, Bliek A |
4501 - 4512 |
Non-linear phenomena during CO oxidation in the mbar pressure range: a comparison between Pt/SiO2 and Pt(100) Lauterbach J, Bonilla G, Pletcher TD |
4513 - 4520 |
The mechanism of kinetic oscillations in the catalytic N2O decomposition over Cu-ZSM-5 Ochs T, Turek T |
4521 - 4527 |
Spontaneous isothermal oscillations in N2O catalytic decomposition: fixed-bed reactor modelling Ciambelli P, Di Benedetto A, Pirone R, Russo G |
4529 - 4533 |
The simple models of critical phenomena in the kinetic region and their parametric analysis Pushkareva TP, Bykov VI |
4535 - 4546 |
Pattern formation in homogeneous and heterogeneous reactor models Sheintuch M, Nekhamkina G |
4547 - 4557 |
Convective instability and its suppression in packed-bed- and monolith reactors Yakhnin VZ, Menzinger M |
4559 - 4566 |
Improved light-off performance by using transient gas compositions in the catalytic treatment of car exhausts Skoglundh M, Thormahlen P, Fridell E, Hajbolouri F, Jobson E |
4567 - 4578 |
Modeling dynamic phenomena in 3-way catalytic converters Koltsakis GC, Stamatelos AM |
4579 - 4588 |
Parametric sensitivity in fixed-bed catalytic reactors with reverse-flow operation Wu H, Rota R, Morbidelli M, Varma A |
4589 - 4602 |
Effect of the intraparticle mass transport limitations on temperature profiles and catalytic performance of the reverse-flow reactor for the partial oxidation of methane to synthesis gas Gosiewski K, Bartmann U, Moszczynski M, Mleczko L |
4603 - 4613 |
The reversed flow operation of a crossflow solid oxide fuel cell monolith Neophytides SG |
4615 - 4627 |
Reverse-flow reactor for a selective oxidation process Ferreira RQ, Costa CA, Masetti S |
4629 - 4638 |
Unsteady-state SO2 converters with inter-stage heat removal Xiao WD, Wang H, Yuan WK |
4639 - 4643 |
Mathematical modeling of unsteady-state operation taking into account adsorption and chemisorption processes on the catalyst pellet Vernikovskaya NV, Zagoruiko AN, Chumakova NA, Noskov AS |
4645 - 4652 |
Practical studies of the commercial flow-reversed SO2 converter Xiao WD, Wang H, Yuan WK |
4653 - 4659 |
Safe operation and control of trickle-bed reactor Hanika J |
4661 - 4667 |
Enlargement of the pulsing flow regime by periodic operation of a trickle-bed reactor Boelhouwer JG, Piepers HW, Drinkenburg AAH |
4669 - 4678 |
Mathematical method for analysis of dynamic processes in chemical reactors Kafarov VV, Mayorga B, Dallos C |