OP-II-3

PP-II-28 Lukianov B.N., Lysikov A.I., Okunev A.G.CATALYTIC SYSTEMS OF HYDROGEN PRODUCTION FOR FUEL-CELLS WITH AREMOVAL OF CARBON DIOXIDE FROM GAS MIXTURE IN SITU.................................. 384PP-II-29 Makarov A.A., Makarov A.M., Ostroushko J.J.OZONE-DESTRUCTION REACTOR BASED ON FOAM POLYURETANWITH PEROVSKIT CATALYTIC LAYER............................................................................. 385PP-II-30 Mehdizadeh H., Sadeghi M.T.MODELING OF METHANE STEAM REFORMING PROCESSIN POROUS CATALYST ..................................................................................................... 386PP-II-31 Mityanina O.E., Kravtsov A.V., Samborskaya M.A.MATHEMATICAL MODELING OF REACTIVE DISTILLATION SYNTHESIS OF MTBE.... 388PP-II-32 Moreira del Rio J., Serrano B., Ortiz A., de Lasa H.EFFICIENCY IN PHOTOCATALYTIC REACTORS: MODELING OF RADIATIONABSORBED BY THE CATALYST ....................................................................................... 390PP-II-33 Mthombeni B., Möller K.P.MODELLING THE EFFECT OF VAPOUR LIQUID EQUILIBRIUMON FISCHER TROPSCH SYNTHESIS PRODUCT DISTRIBUTIONSFOR CONTINUOUS, WELL-MIXED SLURRY REACTORS............................................... 392PP-II-34 Obuchi E., Yanagi K., Kato K., Kuroiwa A., Nakano K.PHOTOCATALYTIC DISINFECTION OF LEGIONELLA PNEUMOPHILAON Ag-DOPED TITANIA THIN FILM................................................................................... 394PP-II-35 Pineda A., Papadaki M.I., Saenz L., Carreto-Vazquez V.H., Rogers W.J., Mannan S.TOWARDS INHERENTLY SAFER REACTOR DESIGN FOR COMPLEX REACTIONS... 396PP-II-36 Potemkin D.I., Snytnikov P.V., Sobyanin V.A.INFLUENCE OF INTERNAL DIFFUSION ON CO PREFERENTIALOXIDATION OVER Cu/CeO 2-x CATALYSTS ....................................................................... 398PP-II-37 Prymyska S., Beznosyk Y., Reschetilowski W.ZEOLITES IN THE GAS PURIFICATION PROCESSES:INVESTIGATION AND SIMULATION.................................................................................. 400PP-II-38 Rattanaphanee P.OPTIMIZATION OF LACTIC ACID-ETHANOL ESTERIFICATIONBY 2 3 FACTORIAL DESIGN OF EXPERIMENTS ............................................................... 402PP-II-39 Rebollar M., Silva E.Y.POLYMERIZATION REACTOR FOR THE EVALUATIONOF CATALYSTS TYPE HONEYCOMB ............................................................................... 404PP-II-40 Reznichenko S., Ratasep M.A., Verigin A.N., Kukushkin M.S., Lebedev S.N.TWO-ROTOR APPARATUS................................................................................................ 406PP-II-41 Sharova E.S., Klimova E.S., Karakulov A.G., Ivanchina E.D.TECHNICAL ECONOMICAL OPTIMIZATION OF INDUSTRIAL REFORMINGREACTOR BY MATHEMATICAL MODELLING .................................................................. 408PP-II-42 Shulayev N.S., Nikolaev Y.A.MICRO REACTORS ON THE PLATFORM OF ROTOR-DISK MIXERS ............................ 410PP-II-43 Sidorova O.I., Galanov S.I.THE AUTOTHERMAL REACTOR OF NATURAL GAS CONVERSIONTO SYNTHESIS GAS ON BASIS OF BLOCK SHS CATALYST......................................... 412PP-II-44 Zhukova O., Stefoglo E.NONISOTHERMAL MATHEMATICAL MODELS FOR FISHER-TROPSCH PROCESSIN THREE - PHASE FLUIDIZED BED ACCOUNTING FOR GAS DISSOLVEDCOMPONENTS CONCENTRATIONS CHANGE IN SUSPENSION DURING THEREACTION. THE PROFIT OF PRELIMINARY INERT LIQUID PRESATURATION BYSYNTHESIS - GAS AND USE THE SPATIAL PACKING FOR GAS - LIQUID FLOWHYDRODYNAMICS IMPROVEMENT ................................................................................. 414630