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George AvgouropoulosFoundation for Research and Technology-Hellas (FORTH), Institute of ChemicalEngineering & High Temperature ChemicalProcesses (ICE-HT)P.O. Box: 1414, Stadiou Str., Platani-RioGR-26504 PatrasGreeceTel.: +30 261 965268 & 272Fax: +30 261 965223E-mail: geoavg@iceht.forth.grJose Luis AyastuyFaculty of Science and Technology,University of the Basque CountrySarriena S/N48080 BilbaoSpainTel.: +34 946 012619Fax: +34 946 013500E-mail: joseluis.ayastuy@ehu.esMaria AyudeINTEMA, UNMdPJuan B. Justo 43027600 Mar del PlataArgentinaTel.: +54 223 481 6600Fax: +54 223 481 6600E-mail: mayude@fi.mdp.edu.arAbulfas BabaevInstitute of Chemical Problems of AzerbaijanNational Academy of Sciences29, H.Javid avenue370143 BakuAzerbaijanTel.: +994 125 105890E-mail: ITPCHT@itpcht.ab.azAlexander BachurikhinLeninsky pr., 47119991 MoscowRussiaTel.: +7 495 121 7931Fax: +7 495 135 8808E-mail: Shao-kahn@yandex.ruTatiana BairachnayaNational Technical University«Kharkov Polytechnic Institute»Frunze str., 2161002 KharkovUkraineTel.: +38 057 707 6661E-mail: Bairachnaya@bigmir.netBair Bal'zhinimaevBoreskov Institute of Catalysis SB RASpr. Akademika Lavrentieva, 5630090 NovosibirskRussiaTel.: +7 383 330 9770Fax: +7 383 330 8056E-mail: balzh@catalysis.ruPredrag BankovicInstitute of Chemistry Technology andMetallurgy, Department of Catalysis andChemical EngineeringNjegoševa 1211000 BelgradeSerbiaTel.: +381-11-2630-213Fax: +381-11-637-977E-mail: predragb@nanosys.ihtm.bg.ac.yuValerii Geirgievich BarabanovRSC «Applied Chemistry»pr. Dobrolubova, 14197198 St. PetersburgRussiaTel.: +7 812 499 9368Fax: +7 812 325 42 87E-mail: vbarabanov@rscac.spb.ruGiuseppe BarbieriITM-CNRVia P. Bucci - c/o UNICAL Cubo 17C87030 Rende CSItalyTel.: +39 098 449 2029Fax: +39 098 440 2103E-mail: g.barbieri@itm.cnr.itDonald BarclaySnap-tite, Inc. Autoclave Engineers Division8325 Hessinger Drive16509 Erie, PennsylvaniaUSAE-mail: donald_barclay@snap-tite.comViktor V. BarelkoInstitute of Problems of Chemical Physics RASAkademika Semenova str., 1142432 Chernogolovka, Moscow regionRussiaTel.: +7 496 522 1817Fax: +7 496 522 1260E-mail: barelko@icp.ac.ruNatalia BaronskayaBoreskov Institute of Catalysis SB RASpr. Akademika Lavrentieva, 5630090 NovosibirskRussiaTel.: +7 383 326 9768Fax: +7 383 330 8056E-mail: baronskaya@catalysis.ru510
Katarzyna BawolakTechnical University of Lodzul. Zeromskiego 11690-924 LodzPolandTel.: +48 426 313117Fax: +48 426 313103E-mail: kbawolak@p.lodz.plDmitriy BelyaninMendeleev University of Chemical Technologyof RussiaMiusskaya sq., 9125047 MoscowRussiaE-mail: lab-tos@mail.ruSergey BeloshapkinUniversity of LimerickMaterials & Surface Science InstitutePlassey Technological Park0000 LimerickIrelandE-mail: serguei.belochapkine@ul.ieNataliya BelyaevaBoreskov Institute of Catalysis SB RASpr. Akademika Lavrentieva, 5630090 NovosibirskRussiaTel.: +7 383 326 9440Fax: +7 383 330 8056E-mail: belyaeva@catalysis.ruAmel BenaddaLaboratoire de Chimie de Gaz Naturel USTHBBP 32 ElAlia Bab Ezzouar16111 AlgiersAlgeriaTel.: +21 350 049773Fax: +21 321 248008E-mail: benaddaamel@yahoo.frSamir BensaidPolitecnico di TorinoCorso Duca Abruzzi, 2410129 TorinoItalyTel.: +39 011 564 4662Fax: +39 011 564 4699E-mail: samir.bensaid@polito.itHeidi BernasLaboratory of Industrial Chemistry and ReactionEngineering, Åbo Akademi UniversityBiskopsgatan 820500 TurkuFinlandE-mail: heidi.bernas@abo.fiDmitriy BokarevLomonosov Moscow State Academy of FineChemical TehnologyVernadsky avenue, 86119571 MoscowRussiaTel.: +7 495 246 4823Fax: +7 495 246 4823E-mail: bokarev_d@mail.ruElisabeth Bordes-RichardUnité de Catalyse et de Chimie du Solide,Université des Sciences et Technologies deLille Cité scientifique59655 Villeneuve d'Ascq cedexFranceTel.: +33 320 434526Fax: +33 320 436561E-mail: elisabeth.bordes@univ-lille1.frDaniel BorioUniversidad Nacional del Sur, UNS – CONICETCamino La Carrindanga Km. 78000 Bahía BlancaArgentinaTel.: +54 291 486 1700 Ext:266Fax: +54 291 486 1600E-mail: dborio@plapiqui.edu.arBoyan BoyanovUniversity of Plovdiv, Departmant of Chemistry24 Tsar Assen str.4000 PlovdivBulgariaTel.: +359 32 261412Fax: +359 32 635049E-mail: boyanb@uni-plovdiv.bgLev BrukLomonosov Moscow State Academy of FineChemical TechnologyVernadsky avenue, 86117571 MoscowRussiaTel.: +7 495 936 8904Fax: +7 495 434 8711E-mail: lbruk@rol.ruValerii BykovBauman Moscow State Technical Unversity2-nd Baumanskaya, 5105005 MoscowRussiaTel.: +7 495 478 0598Fax: +7 495 265 79 05E-mail: vibykov@mail.ru511
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Boreskov Institute of Catalysis of
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Mikhail G. Slinko,Honour ChairmanVa
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PLENARY LECTURES
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PL-1built up from an intrinsic cont
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PL-3DEVELOPMENT OF ZEOLITE-COATED M
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PL-4processes in order to evaluate
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PL-5CATALYTIC PARTIAL OXIDATION OF
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KEY-NOTE PRESENTATIONS
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KN-2GETTING TO THE POINT: FROM MOLE
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KN-3PROBLEMS AND PROSPECTS FOR IMRO
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KN-4remain out of the sight of rese
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KN-5SSITKA allows to study not only
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KN-6individual reaction stages with
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Section 1.Kinetics of catalytic rea
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OP-I-1-specialthat Г s /f changed
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OP-I-3-specialKINETIC MODELING OF L
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OP-I-4PARTIAL OXIDATION OF TOLUENE
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OP-I-5Also, the approach to modelin
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OP-I-6starch granules, but after a
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OP-I-8KINETICS OF CARBON MONOXIDE O
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OP-I-9CHAOTIC DYNAMICS IN THE THREE
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OP-I-10ADSORPTION OF COMPLEX MOLECU
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OP-I-11KINETIC ASPECTS OF METHANE O
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OP-I-12KINETIC STUDIES IN STRUCTURE
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OP-I-13A STUDY ON THERMAL COMBUSTIO
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OP-I-14KINETICS OF THE CONVERSION O
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OP-I-15HYDROCRACKING OF LONG CHAIN
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OP-I-16KINETICS IN THE HYDROGENATIO
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OP-I-17MECHANISM OF FORMATION OF ET
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OP-I-18KINETIC STUDIES OF PROPANE D
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OP-I-19ACTIVITY AND DEACTIVATION OF
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OP-I-20GAS PHASE OXIDATION OF FORMA
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OP-I-21Where k A is the rate consta
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OP-I-22al., 2008; Monolith, 2008).
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OP-I-23Fig. 1. Scheme of the FIM ma
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OP-I-24Θ DZ centersdeactivationr D
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OP-I-25equation [2] to nitrogen iso
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OP-II-1CHEMICAL NANOREACTORS AS BAS
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OP-II-2gas model use, there is no n
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OP-II-3Taking into account these pr
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OP-II-4WATER2METH1STEAM2AOFF3AIR10O
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OP-II-5completely dry, at the same
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OP-II-6Many factors have been found
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OP-II-7mechanistic and kinetic stud
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OP-II-9MODELLING OF DIESEL PARTICUL
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Section 3.Catalytic processesí dev
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OP-III-1BIC’s catalyst for N 2 О
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OP-III-2powder sample with the same
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OP-III-3Analysis of the results sho
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OP-III-4Exhaustaftertreatmenttechno
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OP-III-6SOME PROPERTIES OF PEROVSKI
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OP-III-7with the conventional react
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OP-III-8resistance is the membrane
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OP-III-9mass dispersion and to anal
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OP-III-11PROCESS INTENSIFICATION US
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OP-III-12ETHYL ACETATE SYNTHESIS BY
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OP-III-12products are vaporized and
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OP-III-13The reforming reaction was
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OP-III-14reactivity (compared to ot
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OP-III-15Fig. 2. The spent Smopex-1
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OP-III-16Numbers of curves are acco
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OP-III-17perimeter were determined.
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OP-III-18of 2. MSR has been coupled
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OP-III-19chemisorption heat and pro
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OP-III-20In the experiments, total
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OP-III-21obtained by the new techno
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OP-III-22reactor wall from the two-
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OP-III-23and parameters of synthesi
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OP-III-24Results and discussionThe
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OP-IV-1DEEP DESULPHURIZATION OF PET
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OP-IV-2LACTIC ACID AS A BACKGROUND
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OP-IV-3CO REMOVAL FROM H 2 -rich GA
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OP-IV-4REFORMING OF ETHANOL OVER ME
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OP-IV-5MODELING OF HYDROGEN PRODUCT
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OP-IV-6PRODUCTION OF HYDROGEN FROM
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OP-IV-7SYNTHESIS GAS PRODUCTION FRO
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OP-IV-8HYDROGEN PRODUCTION FROM MET
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OP-IV-9A NEW GENERATION OF SUPER-TH
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OP-IV-10EXERGY ANALYSIS OF ENZYMATI
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OP-IV-11ADVANCEMENT OF SLURRY BUBBL
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OP-IV-12Pd-DOPED PEROVSKITE CATALYS
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OP-IV-13HYDROGEN PRODUCTION VIA MET
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Section 5.Catalytic processing of r
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OP-V-1Scheme 1. The developing path
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OP-V-2An example of the model compo
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OP-V-3catalysts were shown to be su
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OP-V-4Catalyst deactivation was mor
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OP-V-53) Study of the FFAs esterifi
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OP-V-6In the present work, a compre
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OP-V-7Ca 2 Fe 2 O 5 , MgFe 2 O 4 an
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OP-V-8cellulose components decompos
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OP-V-9sintering a couple of spirale
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OP-V-10Catalyst preparationA series
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OP-V-11Catalysts characterizationIn
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OP-V-12Kinetic ExperimentsHexadecan
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OP-V-13DESIGN OF PILOT REACTOR AND
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OP-V-14DEVELOPMENT OF A LAB SCALE C
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OP-V-15DEVELOPMENT OF TWO-STAGE PRO
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OP-V-15The data of Table 2 show, th
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OP-V-17ENERGY PRODUCTION FROM BIOMA
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OP-V-18CATALYTIC PARTIAL OXIDATION
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OP-V-19A PHOTOCATALYTIC REACTOR FOR
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OP-V-20BIOMASS GASIFICATION IN A CA
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OP-V-21ESTIMATION OF OPTIMAL REACTO
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POSTER PRESENTATIONSSection 1. Kine
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PP-I-1CONVERSION OF ETHANOL OVER CO
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PP-I-2LATERAL INTERACTIONS, FINITE
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PP-I-3UTILIZATION OF TAFT EQUATION:
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PP-I-4SELECTIVE HYDROGENATION OF CI
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PP-I-5NON OXIDATIVE REGENERATION ME
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PP-I-6Table 1. Parameters in kineti
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PP-I-7where: k nc , k 1 , k a , k b
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PP-I-8After each adsorption or deso
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PP-I-9The increase in pressure, in
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PP-I-10The analysis of the composit
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PP-I-11The network of βP oxidation
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PP-I-12order of magnitude lower. Th
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PP-I-13ab1,01,0Isotope fraction0,5[
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PP-I-14Relations ‘rate vs alcohol
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PP-I-15[EEAA] t , M[EEAA] t -1 , M
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PP-I-17NEW OSCILLATING REACTION:CAR
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PP-I-18NEW OSCILLATING REACTIONS OF
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PP-I-19KINETICS OF GAS-LIQUID PROCE
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PP-I-20COMPLETE OXIDATION OF HARMFU
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PP-I-21THEORETICAL RESEARCH OF SURF
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PP-I-22INFLUENCE OF ORGANIC HELATES
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PP-I-23The equation of the reaction
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PP-I-25SELECTIVE OXIDATION OF METHA
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PP-I-26coefficients of the equation
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PP-I-27into propionic acid. The giv
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PP-I-28In the studied range of temp
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PP-I-29Table. Reaction temperature
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PP-I-30other in both direction of t
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PP-I-31Reynolds number. The boundar
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PP-I-32NANOPARTICLES AND CATALYSISI
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Section 2.Physico-chemical and math
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PP-II-1For investigation, we used n
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PP-II-2criterion «Zn dissolved in
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PP-II-3exist around the steady stat
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PP-II-4in range 0-1. In our case n
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PP-II-5at comparable activity, the
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PP-II-7CFD-CALCULATION OF MALDISTRI
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PP-II-8INVESTIGATION OF NONLINEAR P
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PP-II-8reactivity. There is a small
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PP-II-10CALCULATION OF INDUSTRIAL C
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PP-II-11type of reactors a catalyst
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PP-II-13MATHEMATTICAL MODELLING OF
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PP-II-13where I Э , M 1Э , M 2Э
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PP-II-14where TOC 0 is the initial
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PP-II-16AUTOCATALYTIC REACTION FRON
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Section 3.Catalytic processesí dev
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PP-III-1for the traditional scheme
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PP-III-2Initial conditions: С i (0
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PP-III-3Afterward, a 30% aqueous hy
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PP-III-4The influence of the water
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PP-III-5Vanadium oxide was grafted
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PP-III-6(T p ) was taken as an inde
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PP-III-7dCdτLABdCNABdτdCdτdCdτd
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PP-III-8O 2 , balanced by He, at a
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PP-III-9Solution of system (3) for
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PP-III-10HDT330ºCHDT350ºCHDT370º
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PP-III-11The activity of Au/support
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PP-III-1249775 m 3 /h0,65Initial te
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PP-III-13through one layer of ACC w
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PP-III-14the runs was always higher
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PP-III-15The experimental data for
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PP-III-16Catalytic hydrogenation of
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PP-III-17The following parameters a
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PP-III-18Figure 1 - Dependence of t
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PP-III-19Our method has some advant
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PP-III-20Furthermore, Ayude et al.
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PP-III-22OPTIMIZATION OF THE METHAN
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PP-III-23EXPERIMENTAL INVESTIGATION
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PP-III-24CATALYTIC REACTORS WITH HY
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PP-III-25ACTIVITY OF Cu/ZSM-5 CATAL
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PP-III-26SIMULATION AND OPTIMISATIO
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PP-III-27model of plug flow reactor
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PP-III-28Calculations were experime
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PP-III-29continuous and pressurized
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PP-III-30adequacy of multistage mod
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PP-III-31+CH 3 OHH 2 O + HO-(CH(CH
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PP-III-32procedure presented by Mar
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PP-III-33HPA-x + 2 H + + Pd 0 ⎯
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PP-III-34of the process as well as
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PP-III-35This study was financially
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PP-III-36phase. Peroxopolyoxometall
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PP-III-37performed under atmospheri
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PP-III-38orders of magnitude larger
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PP-III-39CATALYTIC REACTORS WITH ST
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PP-III-40THE OXIDATIVE DEHYDROGENAT
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PP-III-41MODELLING AND DESIGN OF TH
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PP-III-42COMPLEX TECHNOLOGY OF TREA
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PP-III-43PHOTO ELECTROCHEMISTRY APP
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PP-III-45MODELING OF CATALYTIC α-O
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PP-III-46steady states. It was show
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PP-III-47Results and discussion:The
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PP-III-49FIBROUS PALLADIUM-SUPPORTE
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Section 4.Catalytic technologies in
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PP-IV-1method is adiabatic or autot
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PP-IV-2It had been established that
Page 402 and 403:
PP-IV-4INTERACTION OF ACTIVATED ALU
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PP-IV-5ENVIRONMENTALLY FRIENDLY PRO
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PP-IV-6THE 5%Ni-2%Au/Al 3 CrO 6 SYS
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PP-IV-7MESOPOROUS ANODES BASED ON Y
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PP-IV-8ADVANCED OXIDATION PROCESS F
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PP-IV-9PROCESSING OF POLYMERIC CORD
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PP-IV-10EFFECT OF SULPHUR ON THE CA
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PP-IV-11OXIDATIVE CONVERSION OF MET
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PP-IV-13CATALYTIC FLUE GAS CONDITIO
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PP-IV-14RIBBON POROUS NICKEL BASED
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PP-IV-15ETHANOL CONVERSION TO HYDRO
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PP-IV-16A HIGH-EFFICIENT MICROREACT
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PP-IV-17DIRECT DECOMPOSITION OF NIT
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PP-IV-18NICKEL CATALYSTS BASED ON P
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PP-IV-19SELECTION OF FAVOURABLE FEE
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PP-IV-20FORMALDEHYDE FORMATION DURI
Page 434 and 435:
PP-IV-21PRODUCTION OF HYDROGEN-RICH
Page 436 and 437:
PP-IV-22INFLUENCE OF COMPOSITION OF
Page 438 and 439:
PP-IV-24ONE-STAGE CATALYTIC CONVERS
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PP-IV-25THE STUDY OF METHANE DEHYDR
Page 442 and 443:
PP-IV-26MCM-41-SUPPORTED PdNi CATAL
Page 444 and 445:
PP-IV-27IMPROVING THE FLOW SHEET OF
Page 446 and 447:
PP-IV-29THE PARTIAL OXIDATION OF CH
Page 448 and 449:
PP-IV-30PRODUCTION OF CO-FREE HYDRO
Page 450 and 451:
PP-IV-31PHOTOCATALYTICAL ACTIVITY O
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PP-IV-32NEW ELECTRODE MATERIALSFOR
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PP-IV-33THE CATALYTIC HYDROGENATION
Page 456 and 457:
PP-IV-34W 0, μmol O 2/min0,25 1. 1
Page 458 and 459:
PP-V-1INFLUENCE OF ICE ON MEAs OF P
Page 460 and 461: PP-V-2DIRECT OILS HYDROGENATION TO
Page 462 and 463: PP-V-3DEVELOPMENT OF Pd/SIBUNIT CAT
Page 464 and 465: PP-V-4Pt NANOPARTICLE-HOLLOW POROUS
Page 466 and 467: PP-V-5THE PROCESS FOR PRODUCING ORG
Page 468 and 469: PP-V-6water removing. This method p
Page 470 and 471: PP-V-7ResultsThe presented technolo
Page 472 and 473: PP-V-8the most effective catalysts.
Page 474 and 475: PP-V-9Neither the low sulphur conte
Page 476 and 477: PP-V-10composition (methyl esters,
Page 478 and 479: PP-V-11reactor we can see that its
Page 480 and 481: PP-V-12Recent studies lead in this
Page 482 and 483: PP-V-13catalysts (e.g. Pt or Pd), t
Page 484 and 485: PP-V-14Alkali catalyst. For a basic
Page 486 and 487: PP-V-15obtaining the related profil
Page 488 and 489: PP-V-16reaction parameters, not rep
Page 490 and 491: PP-V-18STUDY OF THE CATALYTIC ACTIV
Page 492 and 493: PP-V-19BIOMORPHIC CATALYSTS ON THE
Page 494 and 495: PP-V-20Al,Cu-PILLARED CLAYS AS CATA
Page 496 and 497: PP-V-21KINETICS OF THE HYDROXYMATAI
Page 498 and 499: PP-V-22THE NEW METHOD OF OBTAINING
Page 500 and 501: PP-V-23containing mono- and di-subs
Page 502 and 503: AUTOCLAVE ENGINEERS COMPANYSYSTEMAT
Page 504 and 505: CATACON CATACON CATACON CATACON CAT
Page 512 and 513: Leonid BykovJSC «Chemphyst-Alloy L
Page 514 and 515: Debora FinoPolitecnico di TorinoCor
Page 516 and 517: Jenő HancsókUniversity of Pannoni
Page 518 and 519: Andrey KhudoshinLomonosov Moscow St
Page 520 and 521: Cristian LedesmaEnergetic Technique
Page 522 and 523: Uri Matatov-MeytalDepartment of Che
Page 524 and 525: Karina OjedaIndustrial University o
Page 526 and 527: Yuri PyatnitskyPisarzhevsky Institu
Page 528 and 529: Vera ScmachkovaBoreskov Institute o
Page 530 and 531: Peter StrizhakPisarzhevsky Institut
Page 532 and 533: Nadezhda VernikovskayaBoreskov Inst
Page 534 and 535: Nataliya ZubritskayaRSC «Applied C
Page 536 and 537: ORAL PRESENTATIONS.................
Page 538 and 539: OP-I-21Saeedizad M., Sahebdelfar S.
Page 540 and 541: OP-III-9Nekhamkina O., Sheintuch M.
Page 542 and 543: OP-IV-5Hernández L., Kafarov V.V.M
Page 544 and 545: OP-V-13Sadykov V., Mezentseva N., V
Page 546 and 547: PP-I-15PP-I-16PP-I-17PP-I-18PP-I-19
Page 548 and 549: PP-II-9 Nikiforov A., Paek U-Hyon,
Page 550 and 551: PP-III-17 Vernikovskaya N.V., Kashk
Page 552 and 553: PP-III-42 Goshu Y.W., Tsaryov Y.V.,
Page 554 and 555: PP-IV-17 Ohnishi C.H., Yoshino H.,
Page 556 and 557: PP-V-9 Hancsók J., Magyar S., Kall
Page 558: XVIII International Conference on C
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