Lectures A

A1 - Monday morning
Reaction engineering

Keynote lecture: A modelling framework based on population balances for optimum operation and advanced control of emulsion polymerization. Alhamad B., Romagnoli J. A., *Gomes V. G. (Univ. Sydney, AU) [1292]

Modelling of the elaboration of high impact polyamide blends synthesis by reactive extrusion. Rached R., Hoppe S., *Pla F. (LSCG, Nancy, FR) [644]

Modification of polymer compositions with blocked polyisocyanates. Kozak N. V., *Kosyanchuck L. F., Menzheres G. Y., Nizelskii Y. M. (Inst. Macromol. Chem., Kyiv, UA) [1093]

Degassing of porous particles of semi-crystalline polyolefins. *Novak A., Bobak M., Kosek J. (Inst. Chem. Technol., Praha, CZ) [1034]

Multizone circulating reactor modeling for gas-phase polymerization. *Fernandes F. A. N., Lona L. M. F.¹ (Univ. Fed. Rio Grande Norte, Natal, BR; ¹Univ Campinas, BR) [84]

Analysis of the dynamic behaviour of the CSTR polymerisation reactor using diferent strategies cooling: jacket and semi-flooded horizontal condenser. *Vasco de Toledo E. C., Maciel Filho R. (UNICAMP, Campinas, BR) [465]

New catalyst for depolymerization of high density polyethylene to fuel. Rouzbehani B., *Sallamie N.¹, Yousefi A. (Pet. Univ. Technol., Abadan, IR; ¹Iran Univ. Sci. Technol., Tehran, IR) [903]

A2 - Monday afternoon
Reaction engineering

Development of a monolithic bioreactor: carbon ceramic composites as carriers for enzyme immobilization. *de Lathouder K. M., Kapteijn F., Moulijn J. A. (Delft Univ. Technol., NL) [527]

Multi-functional unit combining a fuel cell and an enzyme electro-membrane reactor: Concepts, design, experiments. *Kukula R., Schultz T.¹, Schroder T.¹, Sundmacher K.¹, Hasal P. (Inst. Chem. Technol., Praha, CZ; ¹Max-Planck-Inst. Dyn. Compl. Tech. Syst., Magdeburg, DE) [1138]

The insect cell - an effective expression system. *Buchholz R., Hubner H. (Univ. Erlangen-Nuremberg, DE) [1314]

Kinetic modeling and simulation of bioreactor for ethanol production using Saccharomyces cerevisiae yeast isolated from toddy. *Pramanik K. (Nat. Inst. Technol., Warangal, IN) [1325]

Studies on the production of penicillin G acylase using Escherchia coli ATCC11105. *Ravikumar C., Viruthagiri T. (Annamalai Univ., Annamalai Nagar, IN) [1342]

The inhibition of nitrification by reaction intermediates: the modified Anthonisen diagram. *Juliastuti S. R., Baeyens J.¹, Suwarno J., Ismail T., Musfil A. S., Degreve J.² (Inst. Technol., Surabaya, ID; ¹Univ. Antwerpen, BE; ²Cathol. Univ. Leuven, Heverlee, BE) [759]

Lipase catalysed synthesis of biotensides from renewable sources. *del Amor Villa E. M., Wichmann R. (Univ. Dortmund, DE) [275]

Influence of media formulation on the productivity of the bioinsecticide nematode Steinernema carpocapsae, during the monoxenic liquid production. Batalla-Mayoral J., Rodriguez-Hernandez A.-I., *Chavarria-Hernandez N. (Univ. Aut. Estado Hidalgo, Tulancingo, MX) [599]

Study of dextran enzymatic synthesis using maltose as acceptor: yield and molecular weight. *Rodrigues S., Lona L. M. F.¹, Franco T. T.¹ (Univ. Fed. Rio Grande, Natal, BR; ¹Univ. Campinas, BR) [108]

Acetylation of pea isolate in a stirred-tank reactor. *Nasrallah N., Bouchenafa L., Bensmailli A. (USTHB, Bab Ezzouar, DZ) [1064]

Production of fructooligosaccharides catalyzed by immobilized fructosyl transferase. *Csanadi Z., Sisak C. (Univ. Veszprem, HU) [1137]

Production of protease by thermophilic bacteria. *Al-Qodah Z., Daghistani H. (Al-Balqaa Appl. Univ., Amman, JO) [992]

A3 - Tuesday morning
Symposium on microreaction technology for process development and production

Microreaction technology as a way to solve scale-up problems. *Kroschel M., Ehrfeld W., Merkel T. (Ehrfeld Mikrotechnik AG, Wendelsheim, DE) [634]

New plant concepts using methods based on microchemical engineering. *Kirschneck D., Kober M.¹, Wojik A.¹, Marr R.¹ (Microinnova, Graz, AT; ¹Tech. Univ. Graz, AT) [657]

Micro reactor for selective oxidation of CO in low power fuel cell applications. *Cominos V., Hessel V., Hofmann C., Kolb G., Zapf R., Delsman E.¹, de Croon M.¹, Schouten J.¹ (Inst. Mikrotech., Mainz, DE; ¹Eidhoven Univ. Technol., NL) [268]

The usage of microreaction technology in liquid-liquid extraction processes. *Wojik A., Kirschneck D.¹, Kober M., Marr R. (Univ. Technol. Graz, AT; ¹Microinnova, Graz, AT) [416]

Mathematical modelling of ionic micro- and nano-systems. *Snita D., Postler T., Lindner J., Pribyl M., Kosek J., Marek M. (Inst. Chem. Technol., Praha, CZ) [626]

Experiments with micro- and nanostructurized systems under influence of an external electric field. Slouka Z., *Lindner J., Postler T., Snita D. (Inst. Chem. Technol., Praha, CZ) [565]

Principles of rapid polymerase chain reactions: mathematical modeling and experimental verification. *Viljoen H. (Univ. Nebraska, Lincoln, US) [1403]

Application of laboratory micro-reactor in theoretical and applied technological research of steam cracking. *Zamostny P., Belohlav Z., Herink T. (Inst. Chem. Technol., Praha, CZ) [895]

A4 - Tuesday afternoon
Reaction engineering

Numerical simulations of non-isothermal gas absorption with an exothermic reaction. *Pohorecki R., Moniuk W., Molga E. (Warsaw Univ. Technol., PL) [90]

Nonlinear dynamics in reactor separator systems. Zeyer K. P., Kulkarni A. A., *Kienle A.¹ (Max-Planck Inst. Dyn. Kompl. Tech. Syst., Magdeburg, DE; ¹O. von Guericke Univ., Magdeburg, DE) [312]

Investigation of methanol synthesis under transient and steady-state conditions. *Vollbrecht B., Seidel-Morgenstern A. (Otto-von-Guericke Univ., Magdeburg, DE) [608]

Application of transient methods in three-phase catalysis: Asymmetric catalytic hydrogenation. *Toukoniitty E., Maki-Arvela P., Warna J., Salmi T., Murzin D. Y. (Abo Akad. Univ., FI) [335]

An approximate solution for a transient two phase-CSTR with non-linear kinetics. *Valdes Parada F. J., Ochoa Tapia J. A. (Univ. Aut. Metrop. Iztapalapa, Mexico, MX) [93]

Effects of convection on spatiotemporal solutions in a model of a cross-flow reactor. *Travnickova T., Kohout M., Schreiber I., Kubicek M. (Inst. Chem. Technol., Praha, CZ) [391]

Modelling of CO oxidation in digitally reconstructed porous Pt/gamma-Al2O3 catalyst. *Koci P., Stepanek F.¹, Kubicek M., Marek M. (Inst. Chem. Technol., Praha, CZ; ¹Imperial Coll. Sci., London, UK) [430]

Modelling of automotive catalytic converters for diesel engines. *Kryl D., Koci P., Kubicek M., Marek M., Maunula T.¹, Harkonen M.¹ (Inst. Chem. Technol., Praha, CZ; ¹Kemira Ecocat Catalyst R&D, Oulu, FI) [1230]

How to avoid the modelling of interfacial mass transfer in the presence of chemical reactions and interfacial mass transfer effects. Salmi T., *Warna J., Kangas M., Musakka N. (Abo Akad. Univ., FI) [884]

Dynamical regimes in two mass-coupled CSTRs with a chemical pH-oscillatory reaction. *Pesek O., Schreiberova L., Schreiber I. (Inst. Chem. Technol., Praha, CZ) [540]

A mathematical model for deactivation of methanol synthesis catalyst by sintering. Sahebdelfar S., *Kazemeini M.¹ (Nat. Iran. Pet. Co.,Tehran, IR; ¹Sharif Univ. Technol., Tehran, IR) [445]

A simplified method of modeling the fluidized-bed reactor. Al-Hammad A., *Moustafa T., Lin Y. Y. (SABIC, Riyadh, SA) [7]

A5 - Wednesday morning
Reaction engineering

The interaction of chemical reactions and transport: Combined reactors and exchangers. *Churchill S. W. (Univ. Pennsylvania, Philadelphia PA, US) [1336]

Spouted bed reactors for upgrading of wastes. Aguado R., Prieto R., *Gonzalez P., Arabiourrutia M., Olazar M., Bilbao J. (Univ. Pais Vasco, Bilbao, ES) [278]

Hydrogenation of Citral: Slurry or Monolith?. *Mikkola J.-P., Bernechea J. M., Aumo J., Murzin D. Y. (Abo Akad. Univ., FI) [427]

Residence time distribution of solids in a fluidized bed fuel reactor of a chemical-looping combustion prototype. *Kronberger B., Loffler G., Hofbauer H. (Vienna Univ. Technol., Wien, AT) [1166]

Different configurations and upscaling of two-zone fluidized bed reactor for selective oxidation of butane to maleic anhydride. Gascon J., Tellez C., Herguido J., *Menendez M. (Univ. Zaragoza, ES) [1082]

Selective oxidation of olefins by molecular oxygen in a structured reactor. *Lapkin A., Bozkaya B., Plucinski P. (Univ. Bath, UK) [1347]

A Six Flux Model for the estimation of radiant fields in flat heterogeneous photo-reactors. Brucato A., Grisafi F., Montante G.¹, *Rizzuti L., Vella G. (Univ. Palermo, IT; ¹Univ. Bologna, IT) [1380]

Selectivity of wet oxidation in trickle-bed reactor at periodical operation. *Tukac V., Chyba V., Hanika J. (Inst. Chem. Technol., Praha, CZ) [365]

Vortex centrifugal multiphase reactor. *Kuzmin A. O., Parmon V. N., Pravdina M. K.¹, Yavorsky A. I.², Yavorsky N. I.¹ (Boreskov Inst. Catal., Novosibirsk, RU; ¹Inst. Thermophys., Novosibirsk, RU; ²Novosibirsk State Tech. Univ., RU) [779]

Stability and steady states multiplicity in gas-liquid continuous stirred tank reactor with taking into account the temperature influence on gas solubility. *Stefoglo E. F., Kuchin I. V., Kravtsov A. V. (Inst. Coal&Coal Chem., Kemerovo, RU) [725]

Non-oxidative non-catalytic methane conversion to high molecular weight hydrocarbons using dielectric barrier discharge reactor. *Tarverdi M. H., Mortazavi Y., Khodadadi A.-A., Mohajerzadeh S. S. (Univ. Tehran, IR) [958]

Modeling and application of the continuous two impinging streams reactors in heterogeneous liquid-liquid reactions. *Sohrabi M., Zareikar B. (Amirkabir Univ. Technol., Tehran, IR) [153]

A6 - Wednesday afternoon
Reaction engineering

Improved kinetic data from product analysis: A chemometrical approach. *Kubicka D., Ronnholm M., Salmi T., Murzin D. Y. (Abo Akad. Univ., FI) [592]

A new method of processing the time-concentration data of reaction kinetics. Yeow Y. L., *Wickramasinghe S. R.¹, Han B. B., Leong Y. K. (Univ. Melbourne, AU; ¹Colorado State Univ., Fort Collins CO, US) [169]

Heterogeneous photocatalytic degradation of gaseous trichloroethylene: experimental data and new kinetic model. *Demeestere K., De Visscher A.¹, Dewulf J., Van Leeuwen M., Van Langenhove H. (Ghent Univ., BE) [258]

Kinetics of n-butane skeletal isomerization over Pt-H-mordenite. Nieminen V., *Kangas M., Salmi T., Murzin D. Y. (Abo Akad. Univ., FI) [418]

Kinetic modelling of ethane and propane gas phase oxidative dehydrogenation. *Machli M., Boudouris C., Lemonidou A. A. (Aristotle Univ. Thessaloniki, GR) [612]

Production of conjugated linoleic acid by heterogeneous catalysis - kinetic modeling. *Bernas A., Holmbom B., Salmi T., Murzin D. Y. (Abo Akad. Univ., FI) [816]

Reaction intermediates in selective catalytic reduction of NO by propene in the presence of excess oxygen over Pt-loaded zeolite catalysts. *Huuhtanen M. E., Rahkamaa-Tolonen K.¹, Maunula T.¹, Keiski R.-L. (Univ. Oulu, FI; ¹Ecocat Oy, Oulu, FI) [1186]

Oxidation of chlorinated volatile organic compounds (CVOCs) in a bubble column photochemical reactor. In search for a cost-effective reactor design. *Alibegic D., Tsuneda S., Hirata A. (Waseda Univ., Tokyo, JP) [1103]

Synthesis of the amino and alkoxyderivatives sym-triazines containing fragments of sterically hindered phenol. *Yahia F., Melnikova S. F.¹ (Univ. Boumerdes, DZ; ¹St. Petersburg State Univ., RU) [959]

Single step H2S removal using chelated iron solution: reaction kinetics and reactor modeling. *Tavasoli A., Ghalbi Ahangari M., Karimi A., Bakhtiary H. R., Khodagholi M. A. (Res. Inst. Pet. Ind., Tehran, IR) [719]

Kinetic modeling of the catalytic hydrogenation of rapeseed oils. *Taghizadeh M., Ashoori A.¹, Rostami Dehka M.² (Univ. Sci. Technol., Babol, IR; ¹Mazandran Univ., Babol, IR; ²NISOC, Ahwaz, IR) [878]

Kinetics of the esterification reaction of acetic acid with butanol over Amberlyst 15 catalyst. Mallalah F., Ali S., *Mahdi K. (Kuwait Univ., KW) [1004]

A7 - Thursday morning
Reaction engineering

How do HDS catalysts work? New insights in reaction mechanism and active phase using quasi in-situ FTIR. *Vogelaar B. M., van Langeveld A. D., Eijsbouts S.¹, Moulijn J. A. (Delft Univ. Technol., NL; ¹Akzo Nobel Chem., Amsterdam, NL) [88]

Pd-Ag/SiO2 and Pd-Cu/SiO2 cogelled xerogel catalysts for selective hydrodechlorination of 1,2-dichloroethane into ethylene. Lambert S., *Ferauche F., Brasseur A., Pirard J.-P., Heinrichs B. (Univ. Liege, BE) [64]

Nanostructured La-Cr perovskite catalysts for diesel soot combustion. *Fino D., Russo N., Saracco G., Specchia V. (Politech. Torino, IT) [653]

Effective transport properties of the reconstructed porous catalyst carriers. Salejova G., *Kosek J., Nevoral V., Solcova O.¹, Schneider P.¹ (Inst. Chem. Technol., Praha, CZ; ¹Inst. Chem. Proc. Fundam., Praha, CZ) [930]

Investigating the role of pore structure and hydroxyl characteristics on selectivity in enantioselective hydrogenation reactions. *Steiner P., Mantle M. D., Dummer N.¹, Hutchings G. J.¹, Gladden L. F. (Univ. Cambridge, UK; ¹Cardiff Univ., UK) [172]

Selective hydrogenation of cinnamaldehyde over metal supported molecular sieves. *Hajek J., Kumar N., Maki-Arvela P., Salmi T., Murzin D. Y. (Abo Akad. Univ., FI) [331]

Comparison the effects of ruthenium and rhenium on characterization and catalytic properties of cobalt catalyst in Fischer-Tropsch synthesis. *Tavasoli A., Karimi A., Mortazavi Y.¹, Khodadadi A.-A.¹, Sadagiani K., Mousavian M.¹ (Res. Inst. Pet. Ind., Tehran, IR; ¹Univ. Tehran, IR) [179]

Deactivation of microporous catalysts during non-oxidative methane aromatization. *Fila V., Spatenka S., Bernauer B., Sobalik Z.¹ (Inst. Chem. Technol., Praha, CZ; ¹J. Heyrovsky Inst. Phys. Chem., Praha, CZ) [1265]

Support and dispersion effects on activity of platinum catalysts during wet oxidation of organic wastes. *Masende Z. P. G., Kuster B. F. M.¹, Ptasinski K. J.¹, Janssen F. J. J. G.¹, Katima J. H. Y., Schouten J.¹ (Univ. Dar-es-Salaam, TZ; ¹Eidhoven Univ. Technol., NL) [1335]

Pt-containing polymeric catalytic systems in direct L-corbose oxidation to 2-keto-L-gulonic acid. Lakina N., *Sulman E. M., Matveeva V., Sidorov S.¹, Valetsky P.¹, Tsvetkova L.¹, Bronstein L.² (Tver Tech. Univ., RU; ¹Inst. Organoelem. Compds., Moskva, RU; ²Indiana Univ., Bloomington IN, US) [193]

A study on the effect of various promoters on the characteristics of Cu/ZnO/Al2O3 catalyst. Khosravi M. Y., *Ashrafizadeh S. N., Feyzi F. (Iran Univ. Sci. Technol., Tehran, IR) [224]

Synthesis and application of nanophase nickel ferrite catalysts. *Lin K.-S., Kuo C.-L., Kuo I.-F. (Yuan-Ze Univ., Chung-Li, TW) [319]

A8 - Thursday afternoon
Reaction engineering

Intensified ring hydrogenation processes. *Haringa H. (Davy Process Technology, Pratteln, CH) [89]

Sequential hydroprocessing (SHP) for diesel upgrading. *Galiasso T. R. (Univ. Simon Bolivar, Miranda, VE) [65]

Pyrolysis of HDPE in the 450-700 oC range. *Gonzalez P., Aguado R., Prieto R., Olazar M., Bilbao J. (Univ. Pais Vasco, Bilbao, ES) [279]

Improved industrial process of high-octane hydrocarbon and oxygenated motor fuel production. *Pisarenko E. V., Ban A. G., Pisarenko V. N., Novikov M. E., Gordeev L. S. (Mendeleev Univ. Chem. Technol., Moskva, RU) [591]

Test reactions for industrial naphtha reforming catalysts characterisation: comparative behaviour between Sn or Re addition to Pt/Al2O3 catalyst. *Iarra B., Gonzalez-Marcos M. P., Guil J. M.¹, Gutierrez-Ortiz M. A. (Univ. Pais Vasco, Bilbao, ES; ¹Inst. Rocasolano, Madrid, ES) [745]

Hydrogenation of thymol in a trickle bed reactor. *Dudas J., Hanika J.¹, Lepuru J., Barhuysen M. (Bio/Chemtek CSIR, Modderfontein, ZA; ¹Inst. Chem. Proc. Fundam., Praha, CZ) [1073]

Feedstock quality and operational conditions predict FCC product yields. *Mariaca-Dominguez M. E., Rodriguez-Salomon S., Salazar-Sotelo D. (Inst. Mex. Pet., Mexico City, MX) [1129]

Oxydehydrogenation of propane on supported tungstate catalysts. Jibril B. Y., Al-Zahrani S. M., *Abasaeed A. E. (King Saud Univ., Riyadh, SA) [1275]

Development of xylene isomerization process over Pt/ZSM-5. Huang C.-K., Liu S. D., Tsai T.-C.¹, *Wang I. (Nat. Tsing-Hua Univ., Hsinchu, TW; ¹Nat. Univ. Kaohsiung, TW) [1362]

Catalytic reforming with high activity catalyst. Kadhum A.-A. S., *Oun M. A. B., Al-Halluj M. M. (Azzawiya Oil Ref. Co., LY) [486]

Oxidative dehydrogenation of propane over zeolite catalyst in fixed-bed reactor. *Wojcik W., Jagielska E., Mostowicz R., Sadoska T., Dyczewski M., Szarlik S. (Ind. Chem. Res. Inst., Warszawa, PL) [259]

Optimization of direct conversion of methane to methanol in a catalytic fixed bed reactor. *Vafadjoo L., Sohrabi M.¹ (Azad Univ., Tehran, IR; ¹Amirkabir Univ., Tehran, IR) [174]

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