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

OP-III-9Nekhamkina O., Sheintuch M.FRONT VELOCITY AND CRITERION OF TRANSVERSAL PATTERNSIN PACKED-BED REACTORS ........................................................................................... 107OP-III-10Peshnev B.V., Nikolaev A.I., Asilova N.Y.REACTOR FOR CARBON NANOFIBERS SYNTHESYS................................................. 109OP-III-11Kraai G.N., Schuur B., de Vries J.G., Heeres H.J.PROCESS INTENSIFICATION USING A CONTINUOUS HIGHLYINTEGRATED REACTOR-SEPARATOR DEVICE........................................................... 110OP-III-12Smejkal Q., Kolena J., Hanika J.ETHYL ACETATE SYNTHESIS BY COUPLING OF FIXED BED REACTOR ANDREACTIVE DISTILLATION COLUMN – PROCESS INTEGRATION ASPECTS.......... 112OP-III-13Suzuki T., Nakao F., Na-oki I., Miyake T.PREPARATION AND PERFORMANCE OF WALL TUBE REACTOR IN THEREFORMING OF METHANOL........................................................................................... 115OP-III-14Scarpa A., Landi G., Pirone R., Russo G.MICRO-REACTORS FOR THE COMBUSTION OF METHANE..................................... 117OP-III-15Toukoniitty B., Mikkola J.-P., Murzin D.Yu., Salmi T.MICROWAVES AND ULTRASOUND TOWARD PROCESS INTENSIFICATION....... 119OP-III-16Klenov O.P.FLOW IN THE HONEYCOMB CATALYST WITH POROUS WALLS........................... 121OP-III-17Klenov O.P., Chumakova N.A., Pokrovskaya S.A., Sadykov V.A., Noskov A.S.HONEYCOMB CATALYSTS WITH POROUS WALLS: CFD MODELINGOF INTERACTION OF MASS TRANSFER PROCESSESWITH CATALYTIC REACTION......................................................................................... 123OP-III-18Arzamendi G., Diéguez P.M., Montes M., Odriozola J.A., Sousa-Aguiar E.F.,Gandía L.M.METHANE STEAM REFORMING IN A MICROCHANNEL REACTORFOR GTL INTENSIFICATION: A COMPUTATIONAL FLUID DYNAMICSSIMULATION STUDY......................................................................................................... 125OP-III-19Kravtsov A.V., Ivanchina E.D., Abramin A.L., Gyngazova M.S.COMPUTER MODELING OF CATALYTIC REFORMING PROCESSIN MOVING-BED REACTOR WITH CONTINUOUS CATALYSTREGENERATION ................................................................................................................. 127540