II International Symposium on Carbon for Catalysis ABSTRACTS

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KL-4 The strong mesoporous carbons were produced by pyrolysis and activation of cedar nutshells at the selected conditions. The optimal process parameters of wood wastes (hydrolytic lignin, bark, sawdust) integrated carbonization-activation in a catalytic fluidized bed were selected in order to produce the powdery active carbons. Microporous and mesoporous carbons from natural graphites and anthracites The low reactivity of natural graphites and anthracites limits their use for porous carbons production. The influence of chemical modification of de-ashing natural graphites and anthracites of different deposits on the formation of their microporosity at the further steps of thermal treatments was investigated. Data about structural and textural characteristics of intercalated and thermally exfoliated samples of Zavalevsky and Kyshtymsky graphites were obtained with the use of powder X-ray diffraction, SEM and HREM methods and from isotherms of nitrogen and carbon dioxide adsorption. It was found that the applied method of intercalation makes the significant influence on the nano-textural characteristics of exfoliated graphite. Depending on the intercalation conditions the BET surface area of the thermally expanded graphites varies from 12 up to 70 m 2 /g an the pore volume from 0,08 to 0,55 cm 3 g. Carbon supports from Donetsky anthracite (Progress mine) were prepared by consecutive steps of demineralization, chemical modification by HClO 4 and final activation by CO 2 or water-steam at temperature 1123 o C. Depending on conditions of modification and activation the porosity of carbon products ranges from microporous to mesoporous types and their specific surface area varies from 400 to 1000 m 2 /g. Palladium catalysts on carbon supports from plant polymers, natural graphites and anthracites Palladium catalysts were prepared by an impregnation of the carbon supports with a water-alcohol solution of H 2 PdCl 4 . The size and shape of the supported palladium particles and their distribution over the carbon surface were found to depend on the method of the carbon support preparation. The narrow distribution of the pores width in the fiber carbon support from carbonized cellulose promotes the formation of homogeneous distribution of palladium particles with size 4-5 nm on the carbon surface. 26
KL-4 The most regular distribution of supported palladium particles with an average size of about 2 nm was observed for the supports prepared from the chemically modified natural graphites and anthracites. It was established that the activity of such catalysts in the reactions of cyclohexene and hexane-1 hydrogenation varies in wide limits depending on the size, structure and surface distribution of palladium particles and on carbon support texture. 27
Page 1 and 2: Boreskov Institute of Catalysis of
Page 3: ORGANIZING COMMITTEE Chairman: Vlad
Page 7 and 8: CATALYSTS ON CARBON MATERIALS BASIS
Page 9 and 10: PREPARATION OF CARBON FILMS ON CERA
Page 11 and 12: PL-2 polymer gas separation membran
Page 13 and 14: CHARACTERIZATION OF POROUS STRUCTUR
Page 15 and 16: ROLE OF CARBON POROSITY AND FUNCTIO
Page 17: KEYNOTE LECTURES
Page 20 and 21: KL-1 governed by the equation of th
Page 22 and 23: KL-2 NITROGEN DOPED CARBON NANOFIBE
Page 24 and 25: KL-3 CARBON BASED STRUCTURED CATALY
Page 28 and 29: KL-5 NANOSTRUCTURED CARBONS FOR THE
Page 30 and 31: KL-6 THEORY OF MECHANICAL BEHAVIOR
Page 32 and 33: KL-7 MOLECULAR STRUCTURE EFFECT OF
Page 34 and 35: Presentation of FGUP “ENPO Neorga
Page 37 and 38: OP-I-1 COBALT ON CARBON NANOFIBER C
Page 39 and 40: OP-I-1 from 41 to 23 %, while the C
Page 41 and 42: OP-I-2 loading. It is also interest
Page 43 and 44: OP-I-3 5 nm 50 nm Figure 1: PtRu/MW
Page 45 and 46: OP-I-4 As it can be seen, potassium
Page 47 and 48: OP-I-5 [A] ⇔ A+[ ] (5) Kinetic an
Page 49 and 50: Results and discussion OP-I-6 The T
Page 51 and 52: OP-I-7 product selectivity). The an
Page 53 and 54: OP-I-8 After introduction of the me
Page 55 and 56: OP-I-9 Hydrogenations were carried
Page 57 and 58: OP-I-10 activated with CO 2 . In al
Page 59 and 60: OP-I-11 from Jaroszów deposit, Low
Page 61 and 62: OP-I-12 The carbon matrix avoids th
Page 63 and 64: OP-I-13 • thermal destruction of
Page 65 and 66: OP-I-14 hexanol (AA) was anchored t
Page 67 and 68: OP-I-15 removing the physically ads
Page 69 and 70: OP-I-16 surface concentration of HE
Page 71 and 72: Our analysis of the chemical activi
Page 73 and 74: OP-I-18 running. The TEM reveals th
Page 75 and 76: OP-I-19 explore the role of CNF sur
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pH 10 8 6 4 2 0 2 4 6 8 10 ml HCl a
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OP-I-21 resorcinol to catalyst mola
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OP-I-22 AS in the catalysts examine
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OP-I-23 polyfunctional surface cove
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OP-I-24 as sibunite and nanofibrous
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OP-I-25 is a consequence of the mac
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OP-I-27 THE CARBON FILMS ON Pt(111)
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OP-I-28 LASER RAMAN MICRO-SPECTROSC
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OP-I-29 ELECTROCATALYTIC PROPERTIES
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OP-II-1 SYNTHESIS
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OP-II-2 SYNTHESIS,
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TOWARDS LARGE SCALE PRODUCTION OF C
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CO-CARBONIZATION OF POLYMERS - NEW
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OP-II-5 3. Results
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OP-II-6 pore size
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OP-II-7 their adva
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OP-II-8 effect, el
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OP-II-9 Therefore,
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OP-II-10 The dehyd
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OP-II-11 a result
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INVESTIGATION OF THE ELECTROCHEMICA
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SURFACE ELECTROCHEMISTRY OF CARBON
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TEMPLATED SYNTHESIS OF NOBLE METAL
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PROPERTIES AND STRUCTURE OF SORBENT
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CATALYSIS DURING SULPHUR COALS PROC
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ORDERED MESOPOROUS CARBONS SYNTHESI
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PP-I-7 INFLUENCE OF FUNCTIONALIZATI
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PP-I-8 AROMATIZATION OF 5-PHENYL-PI
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N 2 O CONVERSION USING BINARY MIXTU
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PP-I-9 [8] F. Gonçalves, G.E. Marn
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PP-I-10 The Table 1 demonstrates th
Page 141 and 142:
PP-I-11 We suppose that the active
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PP-I-12 Activation with steam promo
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PP-I-13 separation of bundles forme
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PP-I-14 temperature at which the ma
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PP-I-15 Titania was prepared by hyd
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PP-I-16 A B Figure 1. SEM images co
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PP-I-17 the carbon matrix has been
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PP-I-18 0.9 0.8 0.7 0.6 lg (ΔV/ΔR
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PP-I-19 Electron-microscopic studie
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PP-I-20 time on stream increased fr
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CARBON-SUPPORTED 12-MOLYBDOPHOSPHOR
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PP-I-23 CARBON SUPPORTS FOR IMMOBIL
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PP-I-24 example, in the polymer ele
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PP-I-25 of microporous structure wa
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PP-I-26 contain at first. Non-oxida
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PP-I-27 this reaction and that the
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CONTROLLING DIAMETER AND PRESENCE O
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INFLUENCE OF GAS OXIDATIVE TREATMEN
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PP-I-30 EXPERIMENTAL VALUES OF THE
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PP-I-30 Acknowledgements The author
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PP-I-31 suspensions of UFD had low
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PP-I-32 It was detected, that precu
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PP-I-33 consistence of the process,
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PP-I-34 practically identical [2],
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PP-I-35 • surface porosity (P 245
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PP-I-36 (COOH+OH), mg-eq/g 1,8 1,2
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PP-I-37 As one can see in the table
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PP-I-38 hydrogenation (61 o and 65
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PP-I-39 Ensembles №№ 31, 45, 55
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PP-I-40 The pore structure of origi
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PP-I-41 Sr 2+ and Ba 2+ ions are in
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PP-I-42 volume are formed from init
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PP-I-43 30 wt% Pt-15 wt% Ru/NCM cat
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PP-I-44 Figure 1. From left to righ
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PP-I-45 Table 1: Characteristics of
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PP-I-45 The search for alternative
Page 213 and 214:
PP-I-46 zeroth moment expression, w
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PP-I-47 It was revealed, that the i
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PP-I-48 Table 1 Characteristics of
Page 219 and 220:
PP-I-49 4-Carboxybenzaldehyde (4-CB
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PP-I-50 Computational details First
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PP-I-51 The result showed that surf
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PP-II-1 COOH COO(C
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PP-II-2 The result
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PP-II-3 prepared,
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PP-II-4 CNF from b
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PP-II-5 support; t
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PP-II-6 The main p
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PP-II-7 porous net
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PP-II-8 It is note
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PP-II-9 selective
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STABILITY OF A CARBON CATALYST FLUI
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PP-II-11 CARBON FI
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PP-II-12 CATALYTIC
Page 249 and 250:
THE SORBENTS FOR AIR CLEANING PREPA
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MACRO-SHAPING OF CARBON NANOFIBERS
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PP-II-15 MESOPOROU
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PP-II-16 EVALUATIO
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PP-II-16 As it wou
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PP-II-17 with exis
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PP-II-18 Thus, the
Page 263 and 264:
PP-II-19 (NaOH, Cs
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PP-II-20 MEDICAL C
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PP-II-21 Pt /AC an
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PP-II-22 Prelimina
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FACTORS DETERMINING THE CATALYTIC P
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NANOPOROUS CARBON MATERIALS AS EFFE
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CARBON NANOSTRUCTURAL MATERIALS PRO
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GROWTH OF CARBON NANOFIBERS ON META
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ACTIVE CARBON AS SUPPORT FOR IMMOBI
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PP-II-28 USING OF
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AKSOYLU Ahmet Erhan Department of C
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DIDENKO Olga Pisarzhevskii Institut
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KOGAN Victor M. Zelinsky Institute
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NOUGMANOV Evgeniy Lomonosov Moscow
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SERP Philippe INPToulouse 118 Route
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ZAITSEV Yurij P. Institute for Sorp
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steel, Hastelloy C22, Titanium, Tan
Page 297:
Условия эксплуатац
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DONAU LAB MOSCOW ПРОГРАММА
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CONTENT PLENARY LECTURES...........
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OP-I-12 Maldonado-Hódar F.J., Carr
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OP-II-8 Isse A.A.,
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PP-I-21 Karaseva M.S., Perederiy M.
Page 315 and 316:
PP-I-47 Zaitsev Yu., Zhuravsky S.,
Page 317 and 318:
PP-II-21 Özkara S
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II International Symposium on Carbon for Catalysis ABSTRACTS

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