II International Symposium on Carbon for Catalysis ABSTRACTS

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PP-<strong>II</strong>-23 Table. Investigated Reactions, Accelerated by Various Carbon Sorbents Reactions Experimental conditions Catalysts Acid-base Esterification of acetic acid with butyl alcohol Liquid- and vapor-phase synthesis, in static and flow-type circulatory reaction; T=393-723 K, reagent ratio 1:20 to 20:1 FOU, DOU, LOU, BAU o , UT-O, KPKO Esterification of aliphatic acids with glycerol Transesterification of edible fats and their mixtures Hydrolysis of ethyl acetate Dehydration of methanol and isobutanol Hydrolysis of vegetable oil Hydrolysis sucrose, maltose Hydrogenation of vegetable oil Static conditions with agitation under vacuum (1.3.10-3 Pa, 2 h) or in a fluidized bed reactor, T=373-473 The same; beef and pork fat, soya, palm, and sunflower oil Vapor- and liquid-phase hydrolysis at T=423- 673 K in flow-type circulatory reactor and under static conditions (thermostat, agitation, 24 h) Flow-type reactor, 3 h, T= 493-623 K Static conditions, thermostat, agitation, T= 309-323 K, 24 h The same DOU, SKNO, BAU o , and their Na forms DOU, SKNO, BAU o , and their Na forms FOU-H, FOU-Me (Me- Na, Ca, Cu, Zn, Fe, Ni, Co, K, Mg) FOU, DOU SKNO, KAU o , their Zn, F, Co, Mn, and Cu forms Ditto, FOU, DOU Static conditions, agitation with a stream of hydrogen, 1-13 h, T= 433-503 K Ni-containing FOU and DOU carbons Oxidation-reduction Decomposition of H 2 O 2 Static conditions, thermostat, T= 293 and 309 K FAU, BAU, CKT, AR-3, KAU, SKN, KPK, LOU, their Fe, Co, Ni, Mn, Cu, Cr forms, C+Me x O y (Me – Mn, Cr, Ni, Fe, Cu) Decomposition of oxygen compounds of chlorine Decomposition of hydroperoxide of dibenzyl ether Oxidation of cumene Static conditions, agitation in vessels protected from light, T= 295 K Thermostated bubble-type reactor with reflux condenser, 1-6 h, T= 293-323 K Gasometric apparatus, agitation, T= 343 K DOU-Co, DOU-Ni Cation-substituted forms (co, Ni, Mn, Fe, Cu) of DOU, LOU, SKNO SKN, FAU, DOU, UT o , their Cr, Fe, Co, Mn, Cu, Ni-forms Oxidation of H 2 S Stationary reactor, agitation, T = 294-309 SKN, UT o , DOU, and SO 2 Cr, Fe, Co, Mn, Cu, Ni -forms 272
NANOPOROUS CARBON MATERIALS AS EFFECTIVE PREPARATIONS IN MEDICAL PRACTICE PP-<strong>II</strong>-24 Surovikin V.F., Pjanova L.G., Luzjanina L.S. Institute of Hydrocarbons Processing SB RAS, Omsk, Russia e-mail: val@inkat.okno.ru, uglerod@ihpp.okno.ru Carbon hemosorbent VN<strong>II</strong>TU-1 and carbon enterosorbent VN<strong>II</strong>TU-2 (nanoporous (mesoporous) carbon sorbents for medical purpose) have been developed and obtained in the Institute of Hydrocarbons Processing SB RAS. The carbon sorbents obtained on the base of dispersed carbon belong to mesoporous sorbents group. The domination volume of mesopores (the contents mesopores on a surface up to 80%) allows to carry out effective sorption of toxic substances with low and average molecular weight and the molecules size corresponding to the size of sorbent pores. Sorption activity of carbon hemosorbent VN<strong>II</strong>TU-1 in relation to chemical standard markers has been investigated (tab. 1). Table 1. Sorption activity of carbon hemosorbent VN<strong>II</strong>TU-1 in relation to chemical standard markers. Standard marker Molecular weight Elimination from physiological solution, % Methylene blue 319 92-98 Vitamin В 12 1357 88-90 The essentially new technology of medical purpose carbon materials production has been developed and it is completely appropriate to medicine requirements for the new generation of sorbents. The given technology has allowed to obtain sorbents with the set physicochemical properties (tab. 2). Table 2. Physical-chemical characteristics of sorbents. Parameter norm Parameter name Carbon hemosorbent VN<strong>II</strong>TU-1 Carbon enterosorbent VN<strong>II</strong>TU-2 Spherical granule size, mm 0,70-1,00 0,50-1,00 Total pore volume, cm 3 / g 0,30-0,45 0,35-0,55 Adsorption capacity, g/g ___ Not less than 0,03 Iodine number, g/kg 175-245 200-300 Granule resistance to wear, % per minute, not more than 0,30 0,30 273
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Boreskov Institute of Catalysis of
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ORGANIZING COMMITTEE Chairman: Vlad
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CATALYSTS ON CARBON MATERIALS BASIS
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PREPARATION OF CARBON FILMS ON CERA
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PL-2 polymer gas separation membran
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CHARACTERIZATION OF POROUS STRUCTUR
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ROLE OF CARBON POROSITY AND FUNCTIO
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KEYNOTE LECTURES
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KL-1 governed by the equation of th
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KL-2 NITROGEN DOPED CARBON NANOFIBE
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KL-3 CARBON BASED STRUCTURED CATALY
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KL-4 The strong mesoporous carbons
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KL-5 NANOSTRUCTURED CARBONS FOR THE
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KL-6 THEORY OF MECHANICAL BEHAVIOR
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KL-7 MOLECULAR STRUCTURE EFFECT OF
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Presentation of FGUP “ENPO Neorga
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OP-I-1 COBALT ON CARBON NANOFIBER C
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OP-I-1 from 41 to 23 %, while the C
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OP-I-2 loading. It is also interest
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OP-I-3 5 nm 50 nm Figure 1: PtRu/MW
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OP-I-4 As it can be seen, potassium
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OP-I-5 [A] ⇔ A+[ ] (5) Kinetic an
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Results and discussion OP-I-6 The T
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OP-I-7 product selectivity). The an
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OP-I-8 After introduction of the me
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OP-I-9 Hydrogenations were carried
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OP-I-10 activated with CO 2 . In al
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OP-I-11 from Jaroszów deposit, Low
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OP-I-12 The carbon matrix avoids th
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OP-I-13 • thermal destruction of
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OP-I-14 hexanol (AA) was anchored t
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OP-I-15 removing the physically ads
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OP-I-16 surface concentration of HE
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Our analysis of the chemical activi
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OP-I-18 running. The TEM reveals th
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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
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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
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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
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PP-I-49 4-Carboxybenzaldehyde (4-CB
Page 221 and 222: PP-I-50 Computational details First
Page 223 and 224: PP-I-51 The result showed that surf
Page 225 and 226: PP-II-1 COOH COO(C
Page 227 and 228: PP-II-2 The result
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Page 231 and 232: PP-II-4 CNF from b
Page 233 and 234: PP-II-5 support; t
Page 235 and 236: PP-II-6 The main p
Page 237 and 238: PP-II-7 porous net
Page 239 and 240: PP-II-8 It is note
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Page 243 and 244: STABILITY OF A CARBON CATALYST FLUI
Page 245 and 246: PP-II-11 CARBON FI
Page 247 and 248: PP-II-12 CATALYTIC
Page 249 and 250: THE SORBENTS FOR AIR CLEANING PREPA
Page 251 and 252: MACRO-SHAPING OF CARBON NANOFIBERS
Page 253 and 254: PP-II-15 MESOPOROU
Page 255 and 256: PP-II-16 EVALUATIO
Page 257 and 258: PP-II-16 As it wou
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Page 261 and 262: PP-II-18 Thus, the
Page 263 and 264: PP-II-19 (NaOH, Cs
Page 265 and 266: PP-II-20 MEDICAL C
Page 267 and 268: PP-II-21 Pt /AC an
Page 269 and 270: PP-II-22 Prelimina
Page 271: FACTORS DETERMINING THE CATALYTIC P
Page 275 and 276: CARBON NANOSTRUCTURAL MATERIALS PRO
Page 277 and 278: GROWTH OF CARBON NANOFIBERS ON META
Page 279 and 280: ACTIVE CARBON AS SUPPORT FOR IMMOBI
Page 281 and 282: PP-II-28 USING OF
Page 283 and 284: AKSOYLU Ahmet Erhan Department of C
Page 285 and 286: DIDENKO Olga Pisarzhevskii Institut
Page 287 and 288: KOGAN Victor M. Zelinsky Institute
Page 289 and 290: NOUGMANOV Evgeniy Lomonosov Moscow
Page 291 and 292: SERP Philippe INPToulouse 118 Route
Page 293 and 294: ZAITSEV Yurij P. Institute for Sorp
Page 295 and 296: steel, Hastelloy C22, Titanium, Tan
Page 297: Условия эксплуатац
Page 305 and 306: DONAU LAB MOSCOW ПРОГРАММА
Page 307 and 308: CONTENT PLENARY LECTURES...........
Page 309 and 310: OP-I-12 Maldonado-Hódar F.J., Carr
Page 311 and 312: OP-II-8 Isse A.A.,
Page 313 and 314: 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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