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PP-II-37Fig. 1. X-ray diffraction pattern of MgO prepared from thermaldecomposition of magnesium methoxide.References1. K. J. Klabunde (ed.), Nanoscale Materials in Chemistry, John Wiley, 2001.2. M.A. Aramendia, V. Borau, C. Jimenez, J.M. Marinas, Appl. Catal. A, 255 (2003) 301.3. B-Q.Xu, J-M Wei, H-Y Wang, K-Q Sun, Q-M Zhu, Catal. Today 68 (2001) 2174. H.Sung, J. Lee, J. Kim, K. Hong, J. Colloid Interf. Sci. 259 (2003) 127.230
PP-II-38INVESTIGATION OF STRUCTURE AND MORPHOLOGY OF CATALYSTSBASED ON KAZAKHSTANI ALUMOSILICATES ACTIVE IN THE CRACKING OFHEAVY OIL RESIDUESIbrasheva R.Kh., Rakhimov A., Tusupbaev R.Kazakh-British Technical University, Almaty, KazakhstanE-mail: armanrakhimov@gmail.comEnergetic and ecological problems of processing of highly viscous oils requires design ofnew technological solutions. Urgent problem is use of inexpensive and accessible residualfractions from the petrochemical plants. The expediency of the processing of heavy oilfractions by oxidative cracking has been stated in [1]. In contrast to this work, which dealswith the catalysts based on zeolites, the aim of [2] was the oxidative cracking of vacuumgasoils and mazuts carried out on the composites containing both zeolites and clays. Thepeculiarity of the proposed process is in the irreversibility of the used cheap catalyst under itslow consumption. This enables one to dispense the stage of regeneration of the used catalyst,which contributes to the aggravation of ecological indices of the existing industrial processes.The aim of the present work was to investigate the influence the nature of Kazakhstan’szeolites and clays, conditions of their activation and relative concentrations of the componentswhich they have upon the cracking properties of catalysts in the range of reactions ofdestruction of hydrocarbons composing the heavy oil fractions. Chemical composition, thestructure of catalysts, acidity of their active sites have been investigated and determined withthe help of combined usage of XFS-spectroscopy, X-ray diffraction and IR-spectroscopicmethods. It was determined, that the optimal concentration of components of activatedcomposite catalysts does not depend on the nature of zeolites and clays composing theirstructure and is within the interval 14-15 % for zeolites and 86-85 % for clays.231
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"Catalysis is not a branch of chemi
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Siberian Branch of Russian Academy
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INTERNATIONAL ADVISORY COMMITTEE:A.
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POSTER PRESENTATIONSSECTION IMECHAN
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PP-I-1more time in the oxidised sta
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PP-I-2Study of chemical reactions p
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PP-I-3It is suggested that during p
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PP-I-4reaction conditions, 100% con
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PP-I-5Catalytic properties of synth
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PP-I-6iii) The magnitude of above m
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PP-I-8ONE-DIMENSIONAL AND THREE-DIM
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PP-I-8This work was carried out at
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PP-I-9formed on their place. The PI
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PP-I-10CatalystЕа 1 ,kJ/mol(77÷1
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PP-I-11to increase of selectivity t
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PP-I-12The nanostructure of CS (clu
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PP-I-13The exchange in high-tempera
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PP-I-15ROLE OF CARBON DIOXIDE IN TH
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PP-I-16DIRECT OXIDATION OF BENZENE
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PP-I-17DFT STUDY OF REDUCTION REACT
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PP-I-18ORIGINAL MONTE CARLO METHOD
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PP-I-19STUDY ON THE MECHANISM OF TH
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PP-I-20NANOSIZED METAL OXIDES AS ST
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PP-I-21THE STUDYING OF THE NATURE O
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PP-I-22SYNTHESIS OF ETHYLENE-BUTADI
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PP-I-24REACTION OF PHENYLACETYLENE
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PP-I-25EFFECT OF THE PRESSURE ON TH
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PP-I-26INTERPRETATION OF THE ETHYLE
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PP-I-27STUDY OF ONE-POT REDUCTIVE D
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PP-I-28TUNING SURFACE MORPHOLOGY OF
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PP-I-29HIGHLY POROUS BLOCK CELLULAR
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PP-I-30STRUCTURE OF PHOTOCATALYTIC
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PP-I-31According to the 13 C MAS NM
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PP-I-32Conversion and selectivity a
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PP-I-34STUDY OF THE MECHANISM OF CA
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PP-I-35COMPARISON CATALYTIC ACTIVIT
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PP-I-36CRITICAL PHENOMENA FOR LANGM
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PP-I-37ISOTHERMS FOR STEPPED SURFAC
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PP-I-38RESOLUTION OF CHIRAL SULFOXI
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PP-I-39INVESTIGATION OF AMINO-CONTA
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PP-I-40APPLICATION OF POSITRON ANNI
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PP-I-41large pores (15-100 μm) of
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PP-I-42 Pd(1x2) Pd(1x1) Pd(1x2)-c
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PP-I-43the Al/Zr molar ratio has an
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PP-I-44transferred on nickel throug
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PP-I-45S BET , XRD, TPR, SEM, TEM a
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PP-I-46normal and branched alkanes
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PP-I-47growth stages (2) and (3) -
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PP-I-48system operated at frequenci
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PP-I-49The reactivity of these mate
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PP-I-51RECONSTRUCTION OF THE Pd(pol
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PP-I-53INTERMEDIATE PRODUCTS IN PAR
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PP-I-55MOLECULAR MECHANISM OF LOW T
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PP-I-56size of metals encapsulated
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PP-I-57activity of synthetic cataly
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PP-I-58us to suggest that oxidation
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PP-I-59characteristics are as follo
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PP-I-60surfaces changes at 50% cove
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PP-I-611) using the parameter conti
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PP-I-62atoms to PhePA molecule. In
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PP-I-63interaction of CO molecule b
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PP-I-64cases method of Coats-Redfer
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PP-I-65adsorbates and metal atoms.
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PP-I-66were extrapolated then to th
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PP-I-67account an influence of oxyg
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PP-I-68been considered. With this a
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PP-I-70MODIFICATION OF ELECTRONIC S
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PP-I-71most of described methods ch
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PP-I-72Table 1Polymeric active carb
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PP-I-73lower than 450 °C with prac
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PP-I-74Fig. 1. Optimized structure
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PP-I-75(Zn Z d ). The catalytic cyc
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PP-I-76Photocatalytic reaction was
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PP-I-78FRAGMENT COMPOSITION OF DIES
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PP-I-79QUANTUM-CHEMICAL STUDIES OF
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PP-I-80INFUENCE OF CHEMICAL TREATME
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PP-I-81ADSORPTION OF SMALL SILVER S
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PP-I-82EXPLOSION SAFETY IN GAS TRAN
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PP-I-83(ONNO) ad → N 2 O ad + O a
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CATALYTIC ACTIVATION OF UNFAVOURABL
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PP-II-1Therefore, the observed incr
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PP-II-2The samples of uranium oxide
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PP-II-3catalysts prepared by hydrot
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PP-II-4[(C 6 H 5 ) 2 (CH 2 =CHSi] 2
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PP-II-6THE NEW Ni, Zr, Ti-CONTAININ
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PP-II-7SPATIALLY RESOLVED UV-VIS MI
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PP-II-8POLYOL MEDIATED SYNTHESIS OF
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PP-II-8CuO phase were detected, sug
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PP-II-9SHS-INTERMETALLIDES ON THE B
Page 181 and 182: PP-II-10CO OXIDATION IN HYDROGEN ST
Page 183 and 184: PP-II-11CATALYTIC PERFORMANCE OF CO
Page 185 and 186: PP-II-12FORMATION OF RADICAL CATION
Page 187 and 188: CATALYSTS MOLECULAR DESIGN BY SURFA
Page 189 and 190: PP-II-14THE CATALYTIC ACTIVITY OF F
Page 191 and 192: OXIDATION TRIMETHYLHYDROHYNONE IN T
Page 193 and 194: PP-II-16TECHNOLOGY CONCEPTS ON DEVE
Page 195 and 196: ACTIVATION OF POST-TITANOCENE OLEFI
Page 197 and 198: STRUCTURE FEATURES OF NANOCRYSTALLI
Page 199 and 200: THE H 2 ROLE IN SELECTIVE NO X REDU
Page 201 and 202: PP-II-20THE IN SITU FTIR STUDY OF T
Page 203 and 204: PP-II-21LUMINESCENT DIAGNOSTICS OF
Page 205 and 206: PP-II-22MODIFICATION OF PROPERTIES
Page 207 and 208: PP-II-23FTIR STUDY OF THE REACTION
Page 209 and 210: PP-II-24pores (the average diameter
Page 211 and 212: PP-II-25and the amount of the disso
Page 213 and 214: PP-II-27ACTIVITY OF PALLADIUM CATAL
Page 215 and 216: MODIFIED POLYOXIDE CATALYSTS FOR SY
Page 217 and 218: PP-II-29PRODUCTION OF HYDROGENCONTA
Page 219 and 220: INFLUENCE OF COMPOSITION AND STRUCT
Page 221 and 222: PP-II-311NEW COMPOSITE OF A POLYACE
Page 223 and 224: SOME ASPECTS OF THE SELECTION OF ST
Page 225 and 226: PP-II-33HYDROTREATING CATALYSTS MOD
Page 227 and 228: PP-II-34NORBORNADIENE IN NEW SHAPE-
Page 229 and 230: PP-II-36CATALYTIC SYSTEMS BASED ON
Page 231: PP-II-37EFFECT OF PHYSIOCHEMICAL PR
Page 235 and 236: PP-II-38As a result of the combined
Page 237 and 238: PP-II-39synthesized by deposition-p
Page 239 and 240: PP-II-40halogen in NiX 2 (PPh 3 ) 2
Page 241 and 242: PP-II-41fell cell - with the requir
Page 243 and 244: PP-II-42SYNTHESIS OF CATALYSTS ON T
Page 245 and 246: PP-II-43-crucial role play peroxide
Page 247 and 248: PP-II-44According to the obtained d
Page 249 and 250: PP-II-46CYCLOALUMINATION OF α,ω-D
Page 251 and 252: PP-II-47ETHYLENE OLIGOMERIZATION TO
Page 253 and 254: PP-II-48aluminas are in the range o
Page 255 and 256: PP-II-49synthesis methods such as s
Page 257 and 258: PP-II-50Here, we report the first s
Page 259 and 260: PP-II-51hydrogenation. This peculia
Page 261 and 262: PP-II-524% and higher. Apparently t
Page 263 and 264: PP-II-53The secondary methods are b
Page 265 and 266: PP-II-55NOVEL CHIRAL NITROGEN CONTA
Page 267 and 268: PP-II-56NON-OXIDATIVE METHANE CONVE
Page 269 and 270: PP-II-57THE CATALYTIC ACTIVITY OF P
Page 271 and 272: PP-II-58The analysis of the raw mat
Page 273 and 274: PP-II-59analysis. Specific surface
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Page 277 and 278: PP-II-61Deep oxidation of CB vapors
Page 279 and 280: PP-II-62precipitate at 100 o C favo
Page 281 and 282: PP-II-63Х X n-С н-C 6 , %1008060
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PP-II-64mixture by microwave radiat
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PP-II-65and 99.995 % mass.) were sa
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PP-II-66CATALYTIC SYSTEMS BASED ON
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PHASE ANALYSIS OF MULTIELEMENT CATA
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PP-II-68EFFECT OF THE LIGAND SUBSTI
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PP-II-69Results and discussion: The
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PP-II-70tests in POM reaction and T
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PP-II-71The acidity, measured by tw
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PP-II-72The effect of nature and ac
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PP-II-74STUDY OF METHANE DEHYDROARO
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PP-II-75CATALYTIC OXIDATION OF ORGA
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Knowledge of the surface VO x speci
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PP-II-77propylene polymerization on
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THE EFFECT OF THE SUPPORT ON THE PE
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THE ACIDIC CATALYSIS IN REACTION OF
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HYDROGEN-RICH GAS PURIFICATION FROM
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PP-II-82During the stage of combine
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PP-II-83higher H 2 /propane ratios
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NANOSTRUCTURED MATERIALS BASED ON Z
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ELECTROCATALYTIC REDUCTION OF NITRO
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PP-II-87with CuKα radiation (λ ~
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PP-II-88The properties of the catal
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PP-II-89The stereospecificity of po
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PP-II-91SYNTHESIS AND CHARACTERIZAT
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PP-II-92INFLUENCE OF NATURE OF HETE
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PP-II-93OPTICALLY ACTIVE AMMONIUM S
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PP-II-94THE INFLUENCE OF FORMING CO
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PP-II-95NEW CATALYST OF LOW-TEMPERA
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PP-II-96DRIFTS AND UV-VIS STUDY OF
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PP-II-97NANOSTRUCTURED COMPLEX OXID
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PLATINUM CATALYSTS AND THEIR ACTIVI
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PP-II-99DESIGN OF STRUCTURED CATALY
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PP-II-100THE INFLUENCE OF CARBON ON
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PP-II-100sp 2 -carbon samples (Sibu
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PP-II-101Undoped LaMnO 3 has a stru
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PP-II-102The redox mechanisms of ca
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PP-II-103weak surface complexes of
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PP-II-104Ellipsometric, LA-XRD, TEM
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357PP-II-105It follows that MAO (or
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PP-II-106For the description of met
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361PP-II-1070.75, 1) were prepared
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PP-II-108(K⋅10 6 l/mole⋅mg⋅eq
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PP-II-110EFFECTS OF THE PROPERTIES
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PP-II-111CATALYTIC ACTIVITY OF POLY
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SYNTHESIS OF OXIRANES FROM RENEWABL
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PP-II-113SELECTIVE OXIDATION OF FOR
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BIODIESEL PRODUCTION FROM OLEIC ACI
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PP-II-115THE MECHANISM OF PHENOL OX
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PP-II-116THERMOSTABILITY OF Pd-ZEOL
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PP-II-117CO OXIDATION ON CuO-CeO 2
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PP-II-118THE ROLE OF I-CONTAINING P
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PP-II-119THE BULK POROUS ELECTRODE
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PP-II-120Methanol was suggested to
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PP-II-121Synthesis of catalysts on
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Yield, %PP-II-122Dynamics of variat
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PP-II-123The analysis of the hydroc
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PP-II-125THE MECHANISM OF COPPER CO
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PP-II-126The problem of the low act
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PP-II-127size of hydrocatalytic pro
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PP-II-128enhanced stability against
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PP-II-130HYDROGEN PRODUCTION BY MET
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CATALYTIC HYDROALKOXYCARBONYLATION
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NANOSTRUCTURED METAL-POLYMERIC CATA
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PP-II-133THE EFFECT OF THE SUPPORT
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PP-II-134АLTERNATIVE APPROACH TO D
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PP-II-135THE LOW-TEMPERATURE CATALY
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CATALYTIC PROPERTIES OF LAYERED OF
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PP-II-138EFFECT OF Zr ON THE OXIDAT
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PP-II-139THE NATURE OF ACTION OF TH
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PP-II-140CYCLOHEXANE OXIDATION OVER
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PP-II-141Mo AND W HETEROPOLYACID-CO
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HYDROCARBON CONVERSION CATALYSTS BA
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PP-II-142selectivity of the hexene-
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PP-II-143XPS, XRD and UV-Vis DRS st
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PP-II-144from the surface of sample
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PP-II-146THE INFLUENCE OF THE ACIDI
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PP-II-147CHARACTERISATION OF NEW GO
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STUDY ON THE REGULARITIES OF THE FO
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PP-II-148Platinum catalysts support
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PP-II-149selectivity to LHC, moreov
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PP-II-150steamed until a gel format
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PP-II-151ELECTRONIC STATE OF Cr n+
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PP-II-152METAL SUPPORTED CATALYSTS
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PP-II-153FORECASTING CATALYTIC CHAR
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RE - CONTENTING HC OXIDATION CATALY
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PP-II-155reaction are shown on the
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PP-II-156The product of stereoselec
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PP-II-157Supporting Pd on ZnO coate
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PP-II-158relating to acetone. With
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PP-II-159At the same time, catalyst
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PP-II-160The aim of our work is to
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PP-II-161crystallization state of t
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PP-II-162several carbon materials a
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PP-II-1625. J. M. H. Dirkx, H. S. v
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PP-III-1INFLUENCE OF DISSOLVED OXYG
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PP-III-2and microstructure, oxidati
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PP-III-3Aerosol, vapour of toxiccom
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PP-III-4inserted in PAn either in t
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PP-III-5The mechanism of pyrolysis
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ELECTROCATALYSTS WITH LOW PLATINUM
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PP-III-8VERY PURE SILICA FIBROUS AS
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PP-III-9METAL CONTAINING ZEOLITES -
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THE INFLUENCE OF TREATMENT METHOD O
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PARA-HYDROGEN INDUCED POLARIZATION
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PP-III-12NOVEL CHITOSAN-BASED CATAL
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PP-III-13Fig. 1. Dark adsorption (1
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PP-III-14residual pressure of 0.67
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PP-III-15using the same feedstock.
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PP-III-16Fig. 2. SEM-images of surf
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EPOXIDATION OF RAPESEED OIL BY HYDR
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PP-III-19THE PECULIARITIES OF CATAL
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PP-III-20CATALYTIC MEMBRANE CONTACT
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PP-III-21CATALYTIC ACTIVE LAYERS ON
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PP-III-22MODIFICATION OF COMPOUNDED
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EFFECT OF LIQUID POLYKETONE ON THE
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CATALYSTS SEARCH FOR α-METYLBENZYL
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PP-III-25PARTIAL OXIDATION OF PROPA
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PP-III-27BIODIESEL SYNTHESIS BY CAT
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PP-III-28PRODUCTION OF BIO-SYNGAS V
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PP-III-28Fig. 1. Changes in Н 2 an
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PP-III-29Table 1: Texture and adsor
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PP-III-30dimensionless front veloci
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PP-III-31synthesized. Experiments h
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PP-III-32It is established, that cr
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PP-III-33adsorptive catalysts in ad
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PP-III-34turbocompressor and two ca
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PP-III-35The Cu, Ni/ γ -Al 2 O 3 c
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PP-III-36pressure at 800-900 o C. T
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PP-III-370,50Concentration / Vol.-%
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PP-III-38HETEROGENEOUS-CATALYTIC DE
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PP-III-39HYDROISOMERIZATION OF CATA
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METHOD OF CATALYTIC UTILIZATION OF
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PP-III-41Catalytic properties of Fe
Page 551 and 552:
PP-III-42heat in a steam-power unit
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PP-III-43In this way, the content o
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PP-III-45THE ECOLOGIC AND ECONOMIC
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PP-III-46INFLUENCE OF SUPPORT NATUR
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PP-III-47MIGRATION OF SUPPORTED PLA
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Table 2.PP-III-47The [Pt]/[Al] atom
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PP-III-48Under nitrogen atmosphere
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PP-III-49With aim to achieve the ho
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PP-III-50clinoptilolite (Aydag depo
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PP-III-51References1. Balzhinimaev
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PP-III-52Black light UV lamps. The
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USE OF THE NITROGEN-CONTAINING CARB
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PP-III-54CATALYTIC BEHAVIOUR OF VAR
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PP-III-55and sulfur, was spent (fig
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PP-III-56Specific reaction rates of
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PP-III-57special catalyst system wi
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PP-III-59UTILIZATION OF WASTE BIOMA
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MECHANOCHEMISTRY AND MECHANO-CATALY
Page 587 and 588:
PP-III-62CATALYTIC INTENSIFICATION
Page 589 and 590:
PP-III-64ABOUT WHAT MANUFACTURE OF
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PP-III-65OXDATIVE CONVERSION OF HYD
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PP-III-66COMPLEX QUALITY CONTROL SY
Page 595 and 596:
PP-III-67INFLUENCE OF DIFFUSION, SI
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PP-III-68ONE STEP PROCESS FOR HYDRO
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FEATURES OF DRAG FACTOR FOR COMPLEX
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FIXED BED REACTORS WITH GRADIENT CA
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PP-III-70respective variational pro
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PP-III-71Operation at high volumetr
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PP-III-72It was performed the optim
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PP-III-73production stages of refin
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pik⎛N= fi ⎜∑j ∑⎝ j=1Nik,
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PP-III-75three MCP’s. In the seco
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PP-III-76during the reaction. The i
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PP-III-77enthalpy calculated for va
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PP-III-78calculating kinetics of pa
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PP-III-79ventilators 7 and 10, flam
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PP-III-801) C 6 H 5 CH 3 + 2 [YO]
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PP-III-81Δm/m coating, %204060V=0.
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PP-III-82• diameter of its genera
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PP-III-83ΔP,1mm H 2 O/m40023003420
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Concentration, vol.%PP-III-84The ef
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PP-III-85autocatalyst of thermoconv
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PP-III-86The influence of such para
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PP-III-87hydrocarbons increases wit
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AUTOWAVE PROCESSES IN A STATIC CATA
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PP-III-90KINETIC AND THERMODYNAMIC
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PP-III-91which mathematical descrip
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PP-III-93UTILIZATION OF LARGE-SCALE
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CATALYTIC TECHNOLOGY OF UTILIZATION
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PP-III-95PROPERTIES AND ACTIVITY OF
Page 651 and 652:
PREPARATION AND CHARACTERIZATION OF
Page 653 and 654:
PP-III-98The comparison of TPR runs
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ADVERTISEMENT
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PerformancePassionSuccessAutomotive
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Обслуживаемые рынк
Page 662:
Polyurethanes are an integral part
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− prehydrotreating of gasolines a
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Kovalyov E. 123Kovtunov K. 489Kozlo
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List ofparticipantsABRAMOVA Anna Vs
Page 672 and 673:
BOEVA Olga AnatolievnaD.I. Mendelee
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DJEKIC TanjaEindhoven University of
Page 676 and 677:
GIMUNDINOV Shamil AbzalovichD.V. So
Page 678 and 679:
KACHEVSKY Stanislav AndreevichLomon
Page 680 and 681:
KONEV Vasily NikolayevichBoreskov I
Page 682 and 683:
LEDOUX Marc-JacquesCNRS DPI3 Rue Mi
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MIERCZYŃSKI PawełInstitute of Gen
Page 686 and 687:
OBYSKALOVA Elina AnatolievnaBoresko
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REBROV EvgenyEindhoven University o
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SHALAGINA Anastasia EvgenievnaBores
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SPIRIDONOV Alexey AlexeevichBoresko
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VEDYAGIN Alexei Anatol'evichBoresko
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ZAKHARENKO Valery SemenovitchBoresk
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Volume IVolume IICONTENTPOSTER PRES
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PP-I-25 Hocine S., Cherifi O., Bett
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PP-I-52 Timoshenkov S.P., Artemov E
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PP-I-80 Shinkarev V.V., Kuvshinov G
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PP-II-21 Chistoforova N.V., Yelkina
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PP-II-45 Khachani M., Boucetta C.,
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PP-II-68 Malinskaya M.Ju., Sviridov
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PP-II-90 Nikitin V., Mikenas T., Za
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PP-II-114 Sepúlveda J., Santarosa
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PP-II-139 Tkach V.S., Suslov D.S.,
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Section III. Environmental and indu
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PP-III-28 Yakovlev V.A., Kirillov V
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PP-III-52 Shelimov B., Tolkachev N.
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PP-III-77 Mel’gunov M., Kovalev M
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III International Conference“Cata
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III International Conference

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