Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

PP-II-9 Nikiforov A., Paek U-Hyon, Fedorov V.A REACTOR FOR DYNAMIC HIGH PRESSURE-TEMPERATUREREACTIONS IN GAS PHASE............................................................................ 289PP-II-10 Zubritskaya N.G., Barabanov V.G., Trukshin I.G., Babenko Yu.I.CALCULATION OF INDUSTRIAL CATALYTIC REACTOR FOR THESYNTHESIS OF NON-OZONE-DEPLETING SUBSTANCES........................ 290PP-II-11 Makhlin V.A., Zyskin A.G., Evenchik A.S., Pyshkin A.S.,Turygin V.V., Rusanov V.M., Smirnov V.V.TRICKLE-BED CATALYTIC REACTOR DESIGN.MATHEMATICAL MODELING AND MODEL VERIFICATION ................. 291PP-II-12 Anasov A.S.INITIAL CONDITIONS OF NON-CATALYTIC PARTIAL METHANEOXIDATION PROCESS IN ADIABATIC REACTOR ..................................... 293PP-II-13 Gumerov A.М., Ekimova A.M., Davletbaeva I.M.MATHEMATTICAL MODELLING OF THE PROCESSOF OBTAINING ARTIFICIAL DRYING OIL .................................................. 294PP-II-14 Dominguez-Ramos A., Fuente-Martin A., Aldaco R. and Irabien A.LIGNOSULPHONATE TOTAL ORGANIC CARBON TREATMENTUSING ELECTROCHEMICAL OXIDATION .................................................. 297PP-II-15 Samoilov N.A., Mnushkin L.A., Mnushkina O.L.MATHEMATICAL MODELING OF FRACTIONATION STAGEOF REACTIVE DISTILLATION PROCESS FOR THE PRODUCTIONOF ETHYLENE GLYCOL.................................................................................. 299PP-II-16 Zhivonitko V.V., Koptyug I.V.AUTOCATALYTIC REACTION FRONTS PROPAGATIONIN A PACKED-BED REACTOR........................................................................ 300Section 3. Catalytic processes’ development and reactors design:modeling, optimization, new catalyst application ............................................................. 302PP-III-1 Baronskaya N.A., Khassin A.A., Smirnov Е.I., Yurieva T.M.VARIANTS OF THE CATALYST BED WITH CONTROLLEDTEMPERATURE PROFILE IN TUBULAR DEVICE FORTHE SINGLE-STAGE WATER GAS SHIFT PROCESS.................................. 303PP-III-2 Chekantsev N.V., Ivanchina E.D.MATHEMATICAL MODELING OF PENTANE-HEXANE FRACTIONISOMERIZATION PROCESS ON SI-2 CATALYST........................................ 305PP-III-3 Di Giulio S., Faraldi P., Russo N., Fino D., Saracco G., Specchia V.PHOTOCATALYTIC SELF CLEANING SURFACES FOR HOUSEHOLDCOOLING APPLIANCES................................................................................... 307PP-III-4Dobrego K.V., Koznacheev I.A.OPTIMIZATION AND SCALING UP OF THE RECIPROCAL FLOWREACTORS OF FILTRATION COMBUSTION FOR THE TASKS OFPARTIAL OXIDATION OF METHANE AND VOCS OXIDATION .............. 309548