PL-5the possibility of performing semi-continuous reactions and therefore scale-up is enabled. Ingas-liquid-solid reactions ionic liquids have been shown to be highly selective solvents for theC=C double bond hydrogenation of α,β-unsaturated aldehydes to the corresponding saturatedaldehyde. 15 By changing the anion of the ionic liquid or the temperature at which the reactionis performed, it is possible to vary the selectivity and selectivities close to 100 % are possiblewhen using a Pd/C catalyst although the rate is slower than in conventional organic media.Similarly high selectivity has been demonstrated using Pt/graphite catalysts in an ionic liquidmedia for the conversion to the unsaturated alcohol. The ionic liquid system also facilitatesfacile organic solvent extraction or vacuum distillation of the product phase without theremoval of the catalyst and the system shows good recyclability.For the hydrogenation reactions, the catalysis is truly heterogeneous; however, the use of azeolite in the ionic liquid is likely to be homogeneously catalysed. The Friedel-Craftsbenzoylation of anisole has been successfully carried out in [NTf 2 ] - based ionic liquids using arange of zeolites. 16 This reaction is thought to proceed via a homogeneous mechanism,catalysed by HNTf 2 , generated in-situ by the exchange of the cation from the ionic liquid withthe acid proton on the zeolite. The efficiency of this exchange is shown to be temperature andionic liquid dependent. With [C 8 py][BF 4 ], [C 4 mim][BF 4 ] and [C 4 mim][OTf] no reactionoccurs indicating that insufficient concentrations of acids are generated in these cases tofacilitate the reaction. However [P 66614 ][NTf 2 ] does not support sodium exchange and[N 8881 ][NTf 2 ] only exchanges to a small extent and neither therefore facilitate the reaction.The amount of acid generated at the reaction temperature (80 °C) has been quantified usingtitration and sodium exchange experiments with both methods giving comparable resultswhich correlate well with kinetic data.The “zeolite” catalysed benzolyation of anisole has been compared with a homogeneouslycatalysed process using metal triflate and bistriflimides as well as a binary ionic liquid basedon InCl 3 and a chloride ionic liquid. The zeolite catalysed process had the quickest rate;however, it was only recyclable with recalcination of the solid at 500 o C. The homogeneouslycatalysed reactions also showed good rates of reaction and were active for a wide range ofsubstrates. This system was poorly recyclable and the isolated yields low. Thechloroindate(III) ionic liquids were also found to be a versatile reaction media for a widerange of Friedel-Crafts acylation reactions. In addition, the system is catalytic and totallyrecyclable, using an aqueous workup, with no leaching of the indium into the product phase. 1716
PL-5A combination of homogeneous and heterogenous catalysts has been used to facilitate theone-pot synthesis of the fungicide Fenpropimorph via a Heck reaction or an aldolcondensation and then a reductive amination reaction. 18 Although both Heck and aldolprocesses proceed efficiently in the ionic liquid only the aldol pathway may be recycled. Byusing the amine catalyst from the aldol condensation as the reagent in the subsequentreductive amination reaction a highly atom efficient process is possible. A versatile multistepcatalytic synthesis using a single ionic liquid is possible with the ionic liquid able to be easilyrecycled. In contrast using conventional molecular solvents, the separation is more difficultand requires evaporation and recondensation of the solvent.References:1 M. Freemantle, Chem. Eng. News 1998, 76, 32 March 30; J. D. Holbrey andK. R. Seddon, Clean products and processes I, 1999, 223.2 C. E. Song, W. H. Shim, E. J. Roh and J. H. Chio, Chem. Commun., 2000, 1695.3 C. J. Mathews, P. J. Smith and T. Welton, Chem. Commun., 2000, 1249.4 A. J. Carmichael, M. J. Earle, J. D. Holbrey, P. B. McCormac and K. R. Seddon, Org.Lett., 1999, 1, 997.5 C. deBellefon, E. Pollet and P. Grenouillet, J. Mol. Catal., 1999, 145, 1216 A. J. Carmichael, D. M. Haddleton, S. A. F. Bon and K. R. Seddon, Chem. Commun.,2000, 1237.7 M. F. Pinheiro, R. S. Mauler, R. F. deSouza, Macromol. Rapid. Commun., 2001, 22, 425.8 C. Hardacre, J. D. Holbrey, S. P. Katdare and K. R. Seddon, Green Chem., 2002, 4, 143.9 Y. Chauvin, L. Mussman and H. Olivier, Angew. Chem. Int. Ed. Engl., 1995, 34, 2698.10 P. J. Dyson, D. J. Ellis and T. Welton, Can. J. Chem., 2001, 79, 705; P. J. Dyson,D. J. Ellis, D. G. Parker and T. Welton, Chem. Commun., 1999, 25.11 P. W. N. M. vanLeeuwen, P. C. J. Kamer, J. N. H. Reek and P. Dierkes, Chem. Rev.,2000, 100.12 D. Zim, R. F. deSouza, J. Dupont and A. L. Monteiro, Tet. Lett., 1998, 39, 7071.13 For example, T. Welton, Chem. Rev., 1999, 99, 2071, C. M. Gordon, Appl. Catal., 2002,A222, 101; D. Zhao, M. Wu, Y. Kou, and E. Min, Catal. Today, 2002, 1, 2654;R. Sheldon, Chem. Commun., 2001, 2399; J. Dupont, R. F. de Souza and P. A. Z. Suarez,Chem. Rev., 2002, 102, 3667; Ionic Liquids in Synthesis, ed. T. Welton andP. Wasserscheid, Wiley-VCH: Weinheim, 2003.14 S. Doherty, P. Goodrich, C. Hardacre, H.K. Luo, D.W. Rooney, K.R. Seddon andP. Styring Green Chem. 2004, 6, 63.15 K. Anderson, P. Goodrich, C. Hardacre, D.W. Rooney, Green Chem., 2003, 5, 448.16 C. Hardacre, S.P. Katdare, D. Milroy, P. Nancarrow, D.W. Rooney and J.M. Thompson,J. Catal., 2004, 227, 44.17 M.J. Earle, U. Hakala, C. Hardacre, J. Karkkainen, B.J. McAuley, D.W. Rooney,K.R. Seddon, J.M. Thompson and K. Wahala, Chem. Commun., 2005, 903.18 P.N. Davey, S.A. Forsyth, H.Q.N. Gunaratne, C. Hardacre, A. McKeown, S.E.J. McMath,D.W. Rooney, K.R. Seddon, Green Chem., 2005, 7, 224; S.A.Forsyth, H.Q.N. Gunaratne,C. Hardacre, A. McKeown and D.W. Rooney, Org. Proc. Res. Dev., 2006, 10, 94.17
- Page 1: Сибирское отделени
- Page 5: PLENARY LECTURES
- Page 8 and 9: PL-1“nucleophily”, “electroph
- Page 10 and 11: PL-2This presentation will focus on
- Page 12 and 13: PL-3NOBLE METALS CONTAINING CATALYS
- Page 14 and 15: PL-4KINETICS AND MECHANISM OF SELEC
- Page 18 and 19: PL-6MULTINUCLEAR NMR IMAGING IN CAT
- Page 20 and 21: PL-6At the same time, other excitin
- Page 23 and 24: KS-I-1THE EFFECTS OF ACTIVE SITE CO
- Page 25 and 26: С 2 -С 3 OLEFIN PRODUCTION PATHWA
- Page 27 and 28: - process (3) can be important in t
- Page 29 and 30: OOOOZ mO OXOO XO nYO O n-2(I) HY(II
- Page 31 and 32: KS-I-4В настоящей раб
- Page 33 and 34: TAP-APPROACH IN CATALYTIC MECHANISM
- Page 35 and 36: KS-I-6pressure study. For this inve
- Page 37 and 38: NEW ADVANCED CATALYSTS ON THE BASIS
- Page 39 and 40: KS-II-1Многочисленны
- Page 41 and 42: KS-II-2The following approaches tha
- Page 43 and 44: KS-II-4KINETIC FEATURES AND MECHANI
- Page 45 and 46: KS-II-4от характера ли
- Page 47 and 48: KS-II-5В работе проана
- Page 49 and 50: KS-II-6Me 3 , 1,2,4-Me 3 , Me 4 ).
- Page 51 and 52: KS-III-1INTENSITY OF IR-ADSORPTION
- Page 53 and 54: APPLICATION OF SURFACE SCIENCE PHYS
- Page 55 and 56: KS-III-2преимуществом
- Page 57 and 58: KS-III-3ON THE REGULARITIES OF THE
- Page 59 and 60: KS-III-3пропилена, то н
- Page 61 and 62: KS-III-4K on the same sites that ac
- Page 63 and 64: KS-III-5комплекс вопро
- Page 65: CAN QUANTUM CHEMISTRY HELP TO TAYLO
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OP-I-1MECHANISMS OF HETEROGENEOUS C
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OP-I-2Рис. 1. Зависимос
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CARBON OXIDE HYDROGENATION OVER Fe-
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OP-I-3значения полос
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OP-I-4цеолита, а при с
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IRON EFFECT UPON ALKANES CRACKING O
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OP-I-5На поверхности
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OP-I-6acidity measurements of the H
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OP-I-7Н 2 -D 2 обмен иссл
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OP-I-8NOVEL WAY TO THE SYNTHESIS OF
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OP-I-8глиоксалю - сост
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OP-I-9their intensities, new appear
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OP-I-10activity even with platinum.
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OP-I-10part of CPSS was straightfor
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OP-I-11Однако при гидр
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OP-I-12MOLECULAR MECHANISM OF THE L
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OP-I-12по сравнению с
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OP-I-13over other catalysts in fine
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OP-I-14поперек и под у
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OP-I-15After performing an ageing t
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OP-I-16oxidized to Sn 4+ [4,5]. In
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OP-I-17INFLUENCE OF THE LATTICE OXY
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OP-I-18NEW CATALYST OF LOW-TEMPERAT
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OP-I-19COMPARATIVE STUDY OF METHANE
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OP-I-19syngas selectivity is due to
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OP-I-20EFFECT OF OXYGEN MOBILITY ON
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селективности. В эт
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OP-I-21поликристаллич
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OP-I-22SELECTIVE СО OXIDATION: RE
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OP-I-22Как видно из ри
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OP-I-23установлению к
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OP-I-24CATALYTIC PERFORMANCE OF COP
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OP-I-25MECHANISMS OF METHANE CHLORI
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OP-I-25При исследован
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OP-I-26За модельные мо
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OP-I-27INFLUENCE OF SECOND METAL AD
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OP-I-28ACTIVITY AND DEACTIVATION OF
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OP-I-28а содержание бе
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OP-I-29хлористого вод
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THE MECHANISM OF CHLORINE GENERATIO
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OP-I-30Значения конст
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OP-I-31ТХБ, растворите
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OP-I-32Наряду с хлорид
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CATALYTIC TRANSFORMATIONS OF ALIPHA
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OP-I-34STRONG METAL-SUPPORT INTERAC
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OP-I-34The reduction extent of Ni 2
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OP-I-35impregnating solutions for c
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FEATURES OF CATALYSTS EMPLOYMENT FO
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OP-I-361 - NH 3 (14,5), H 2 S (4,1)
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OP-I-37В условиях реак
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OP-I-38ROLE OF REDOX- AND ACIDIC CE
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OP-I-38Таблица 2. Актив
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OP-I-39Таблица 1. Влиян
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OP-I-40гидроксосилика
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OP-I-41(рис.1). Дегидрир
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PROTON TRANSFER REACTIONSIN TRANSIT
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OP-II-1elucidation of the mechanism
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OP-II-2oscillations of E Pt and pH
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OP-II-3гексана в польз
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OP-II-3более мягкий пу
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R 1OCa 2+OH -OHR 2Рис. 1. Пер
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STUDY OF THE MECHANISM OF CATALYTIC
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MECHANISM OF PHENOL AND ANILINE ALK
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OP-II-7MECHANISM OF FORMATION OF HY
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OP-II-8CATALYTIC AND PHYSICOCHEMICA
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OP-II-8To sum up we can say that Pt
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OP-II-9величины изоме
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OP-II-9увеличением со
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OP-II-10the second metal are still
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OP-II-11которых химизм
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OP-II-116. Co(Ni)Mo-катализ
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OP-II-12гг-1, которая от
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OP-II-13ROLE OF THE SOLVENT IN THE
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OP-II-14KINETICS AND MECHANISM OF P
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O 2H 2 OFeX 2FeX 3I 2HIBuOHP n , Zn
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OP-II-15capable of asymmetric oxida
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OP-II-16Систематическ
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OP-II-17MECHANISM OF ETHYLENE METHO
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OP-II-18MECHANISM OF LIQUID-PHASE C
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OP-II-18катализатора и
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OP-II-19Основным недос
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OP-II-19Литература:1 Шн
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OP-II-20Surprising is the finding t
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OP-II-21ºC) [7]. Полученн
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OP-II-21Настоящая рабо
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OP-II-22W(VI), Ti(IV), Re(VII), х
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OP-II-23MECHANISM OF ACTIVATION AND
- Page 243 and 244:
OP-II-23содержащей сис
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2+2+OP-II-24O25 31 (R=Me)OORD 2/ Ru
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OP-II-25ASYMMETRIC HYDROGENATION OF
- Page 249 and 250:
MECHANISM OF TRIMETHYLPENTANE AND D
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OP-II-26СХЕМА 3. Наибол
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OP-II-27диенофилов - ма
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OP-II-28H 2 MoO 4 и FeMoO 4 поз
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OP-II-29THE CATALYTIC ACTION OF AMM
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OP-II-29Как и в случае
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THE KINETICS AND MECHANISM OF P-TOL
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OP-II-30PhCH-CH 2O+SHKk1 +PhCH-CH 2
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OP-II-31Согласно данны
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OP-II-32TRANSFORMATION OF SULFUR OR
- Page 269 and 270:
Рисунок 1OP-II-32269
- Page 271 and 272:
OP-II-33скорость образ
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FCC GASOLINE SULFUR REDUCTION ADDIT
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OP-II-35NOVEL HETEROGENIZED NICKEL
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OP-II-35повышена до 60-80
- Page 279 and 280:
OP-II-36provide stable experimentat
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DISCRIMINATION OF KINETIC MODELS OF
- Page 283 and 284:
OP-II-37Однако при уве
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OP-II-38Для этих систе
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OP-II-39раскрывается п
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OP-II-40TITANIUM-MAGNESIUM CATALYST
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OP-II-41MECHANISM OF BUTADIENE POLY
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OP-II-41Нами установле
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OP-II-42тщательно пром
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OP-II-43обрыва или пер
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OP-II-44MECHANISMS OF HIGHER α-OLE
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OP-II-44С учётом разни
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OP-II-45сополимеры, пр
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OP-III-1Разбавление аз
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OP-III-1Из таблицы 1 ви
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OP-III-2OPERANDO INFRARED STUDY OF
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OP-III-2with formation of diketene
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OP-III-3С этих позиций
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OP-III-4центров двух т
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OP-III-5аналогов, соде
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OP-III-6QUANTUM-CHEMICAL STUDY OF T
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OP-III-6Hn(H 2 C) ON BHH 3 BBH 3HPh
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OP-III-7положения заме
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OP-III-8поверхностног
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OP-III-9поверхностных
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OP-III-11THERMODYNAMIC CHARACTERIST
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OP-III-11which corresponds to ΔS°
- Page 336 and 337:
OP-III-12i[ Cp2ZrHCl⋅2] 2iiX6= HA
- Page 338 and 339:
OP-III-13MOLECULAR MECHANISM OF 1,2
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OP-III-13changes to the formation o
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OP-III-14Рис. Синергиче
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OP-III-15Содержание во
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OP-III-16XPS AND NEXAFS IN-SITU INV
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OP-III-17THERMAL STABILITY OF GOLD
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OP-III-17Там, где спека
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OP-III-18Окисление Н 2 .
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OP-III-18режима протек
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OP-III-19палладия адсо
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OP-III-20THE ADSORBED OXYGEN SPECIE
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OP-III-20Воздействие н
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OP-III-21and selective oxidation of
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OP-III-22STM/XPS STUDY OF MODEL CAT
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OP-III-22Разработанная
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OP-III-23Образцы редко
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OP-III-24IN SITU GAS-PHASE X-RAY PH
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OP-III-24Перед каталит
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OP-III-25width ΔH = 7-100G. The pa
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OP-III-26структуры, но
- Page 378 and 379:
OP-III-27скорости реак
- Page 380 and 381:
OP-III-28STUDIES OF THE MECHANISM O
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OP-III-28и (iv) повторной
- Page 384 and 385:
OP-III-29При Т
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OP-III-30ACTIVE PHASE TRANSFORMATIO
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OP-III-30- Au, above 650° and for
- Page 390 and 391:
OP-III-31с участием раз
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OP-III-32- high-activity zone - in
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OP-III-33MATHEMATICAL MODEL OF THE
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OP-III-33a) b)Temperature [K]Pressu
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OP-III-34В настоящем со
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OP-III-35кластера имее
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OP-III-36APPLICATION OF MULTINUCLEA
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OP-III-36simultaneous occurrence of
- Page 406 and 407:
OP-III-37металлических
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OP-III-38METHODS FOR INVESTIGATION
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OP-III-39CIDNP IN ANALYSIS OF RADIC
- Page 412 and 413:
OP-III-39солей переход
- Page 414 and 415:
OP-III-40similar π-alkyne CpNi( Ph
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OP-III-41взаимодействи
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MECHANISM OF ARYLHALIDES CATALYTIC
- Page 421 and 422:
YP-1Из полученных да
- Page 423 and 424:
YP-2В развитие указа
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INVESTIGATION OF THE INFLUENCE OF C
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Таблица 1. Диаметр п
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YP-4При использовани
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YP-5В этой связи пред
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N-PENTANE ISOMERIZATION AT THE SUPE
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CYCLOHEXANOL CONVERTION OVER Cu-CON
- Page 437 and 438:
YP-7основных центров
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YP-8Разработана преп
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YP-9размер наночасти
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YP-10фольги очищалас
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YP-11STUDIES OF SELECTIVE HETEROGEN
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YP-11быстрее потенци
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YP-12водорода происх
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YP-13CATALYTIC ACTIVITY AND PHYSICO
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YP-13Hydrogen consumption [a.u.]543
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KS-I-6 Zemlyanov D., Aszalos-Kiss B
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OP-I-8 Magaev O.V., Fedotova M.P.,
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OP-I-30 Rozdyalovskaya T.A., Chudin
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OP-II-12 Lavrenov A.V., Duplyakin V
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OP-II-37 Балаев А.В., Гр
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OP-III-16 Beloshapkin S., Zemlianov
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OP-III-40 Saraev V.V., Kraikivskii
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VII РОССИЙСКАЯ КОНФЕ