Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

More documents

Recommendations

Info

PP-V-23containing mono- and di-substituted isomers is essentially obtained at temperatures 340-350 °C and WHSV= 0.9-1.2 h –1 , the resulting product possesses high cetane number (>80) [1]and good temperature characteristics, in this case pour point of the product is as low as
ADVERTISEMENT
Page 1 and 2:
Boreskov Institute of Catalysis of
Page 3 and 4:
Mikhail G. Slinko,Honour ChairmanVa
Page 5 and 6:
PLENARY LECTURES
Page 7:
PL-1built up from an intrinsic cont
Page 10 and 11:
PL-3DEVELOPMENT OF ZEOLITE-COATED M
Page 12 and 13:
PL-4processes in order to evaluate
Page 14 and 15:
PL-5CATALYTIC PARTIAL OXIDATION OF
Page 16 and 17:
KEY-NOTE PRESENTATIONS
Page 18 and 19:
KN-2GETTING TO THE POINT: FROM MOLE
Page 20 and 21:
KN-3PROBLEMS AND PROSPECTS FOR IMRO
Page 22 and 23:
KN-4remain out of the sight of rese
Page 24 and 25:
KN-5SSITKA allows to study not only
Page 26 and 27:
KN-6individual reaction stages with
Page 28 and 29:
Section 1.Kinetics of catalytic rea
Page 30 and 31:
OP-I-1-specialthat Г s /f changed
Page 32 and 33:
OP-I-3-specialKINETIC MODELING OF L
Page 34 and 35:
OP-I-4PARTIAL OXIDATION OF TOLUENE
Page 36 and 37:
OP-I-5Also, the approach to modelin
Page 38 and 39:
OP-I-6starch granules, but after a
Page 40 and 41:
OP-I-8KINETICS OF CARBON MONOXIDE O
Page 42 and 43:
OP-I-9CHAOTIC DYNAMICS IN THE THREE
Page 44 and 45:
OP-I-10ADSORPTION OF COMPLEX MOLECU
Page 46 and 47:
OP-I-11KINETIC ASPECTS OF METHANE O
Page 48 and 49:
OP-I-12KINETIC STUDIES IN STRUCTURE
Page 50 and 51:
OP-I-13A STUDY ON THERMAL COMBUSTIO
Page 52 and 53:
OP-I-14KINETICS OF THE CONVERSION O
Page 54 and 55:
OP-I-15HYDROCRACKING OF LONG CHAIN
Page 56 and 57:
OP-I-16KINETICS IN THE HYDROGENATIO
Page 58 and 59:
OP-I-17MECHANISM OF FORMATION OF ET
Page 60 and 61:
OP-I-18KINETIC STUDIES OF PROPANE D
Page 62 and 63:
OP-I-19ACTIVITY AND DEACTIVATION OF
Page 64 and 65:
OP-I-20GAS PHASE OXIDATION OF FORMA
Page 66 and 67:
OP-I-21Where k A is the rate consta
Page 68 and 69:
OP-I-22al., 2008; Monolith, 2008).
Page 70 and 71:
OP-I-23Fig. 1. Scheme of the FIM ma
Page 72 and 73:
OP-I-24Θ DZ centersdeactivationr D
Page 74 and 75:
OP-I-25equation [2] to nitrogen iso
Page 76 and 77:
OP-II-1CHEMICAL NANOREACTORS AS BAS
Page 78 and 79:
OP-II-2gas model use, there is no n
Page 80 and 81:
OP-II-3Taking into account these pr
Page 82 and 83:
OP-II-4WATER2METH1STEAM2AOFF3AIR10O
Page 84 and 85:
OP-II-5completely dry, at the same
Page 86 and 87:
OP-II-6Many factors have been found
Page 88 and 89:
OP-II-7mechanistic and kinetic stud
Page 90 and 91:
OP-II-9MODELLING OF DIESEL PARTICUL
Page 92 and 93:
Section 3.Catalytic processesí dev
Page 94 and 95:
OP-III-1BIC’s catalyst for N 2 О
Page 96 and 97:
OP-III-2powder sample with the same
Page 98 and 99:
OP-III-3Analysis of the results sho
Page 100 and 101:
OP-III-4Exhaustaftertreatmenttechno
Page 102 and 103:
OP-III-6SOME PROPERTIES OF PEROVSKI
Page 104 and 105:
OP-III-7with the conventional react
Page 106 and 107:
OP-III-8resistance is the membrane
Page 108 and 109:
OP-III-9mass dispersion and to anal
Page 110 and 111:
OP-III-11PROCESS INTENSIFICATION US
Page 112 and 113:
OP-III-12ETHYL ACETATE SYNTHESIS BY
Page 114 and 115:
OP-III-12products are vaporized and
Page 116 and 117:
OP-III-13The reforming reaction was
Page 118 and 119:
OP-III-14reactivity (compared to ot
Page 120 and 121:
OP-III-15Fig. 2. The spent Smopex-1
Page 122 and 123:
OP-III-16Numbers of curves are acco
Page 124 and 125:
OP-III-17perimeter were determined.
Page 126 and 127:
OP-III-18of 2. MSR has been coupled
Page 128 and 129:
OP-III-19chemisorption heat and pro
Page 130 and 131:
OP-III-20In the experiments, total
Page 132 and 133:
OP-III-21obtained by the new techno
Page 134 and 135:
OP-III-22reactor wall from the two-
Page 136 and 137:
OP-III-23and parameters of synthesi
Page 138 and 139:
OP-III-24Results and discussionThe
Page 140 and 141:
OP-IV-1DEEP DESULPHURIZATION OF PET
Page 142 and 143:
OP-IV-2LACTIC ACID AS A BACKGROUND
Page 144 and 145:
OP-IV-3CO REMOVAL FROM H 2 -rich GA
Page 146 and 147:
OP-IV-4REFORMING OF ETHANOL OVER ME
Page 148 and 149:
OP-IV-5MODELING OF HYDROGEN PRODUCT
Page 150 and 151:
OP-IV-6PRODUCTION OF HYDROGEN FROM
Page 152 and 153:
OP-IV-7SYNTHESIS GAS PRODUCTION FRO
Page 154 and 155:
OP-IV-8HYDROGEN PRODUCTION FROM MET
Page 156 and 157:
OP-IV-9A NEW GENERATION OF SUPER-TH
Page 158 and 159:
OP-IV-10EXERGY ANALYSIS OF ENZYMATI
Page 160 and 161:
OP-IV-11ADVANCEMENT OF SLURRY BUBBL
Page 162 and 163:
OP-IV-12Pd-DOPED PEROVSKITE CATALYS
Page 164 and 165:
OP-IV-13HYDROGEN PRODUCTION VIA MET
Page 166 and 167:
Section 5.Catalytic processing of r
Page 168 and 169:
OP-V-1Scheme 1. The developing path
Page 170 and 171:
OP-V-2An example of the model compo
Page 172 and 173:
OP-V-3catalysts were shown to be su
Page 174 and 175:
OP-V-4Catalyst deactivation was mor
Page 176 and 177:
OP-V-53) Study of the FFAs esterifi
Page 178 and 179:
OP-V-6In the present work, a compre
Page 180 and 181:
OP-V-7Ca 2 Fe 2 O 5 , MgFe 2 O 4 an
Page 182 and 183:
OP-V-8cellulose components decompos
Page 184 and 185:
OP-V-9sintering a couple of spirale
Page 186 and 187:
OP-V-10Catalyst preparationA series
Page 188 and 189:
OP-V-11Catalysts characterizationIn
Page 190 and 191:
OP-V-12Kinetic ExperimentsHexadecan
Page 192 and 193:
OP-V-13DESIGN OF PILOT REACTOR AND
Page 194 and 195:
OP-V-14DEVELOPMENT OF A LAB SCALE C
Page 196 and 197:
OP-V-15DEVELOPMENT OF TWO-STAGE PRO
Page 198 and 199:
OP-V-15The data of Table 2 show, th
Page 200 and 201:
OP-V-17ENERGY PRODUCTION FROM BIOMA
Page 202 and 203:
OP-V-18CATALYTIC PARTIAL OXIDATION
Page 204 and 205:
OP-V-19A PHOTOCATALYTIC REACTOR FOR
Page 206 and 207:
OP-V-20BIOMASS GASIFICATION IN A CA
Page 208 and 209:
OP-V-21ESTIMATION OF OPTIMAL REACTO
Page 210 and 211:
POSTER PRESENTATIONSSection 1. Kine
Page 212 and 213:
PP-I-1CONVERSION OF ETHANOL OVER CO
Page 214 and 215:
PP-I-2LATERAL INTERACTIONS, FINITE
Page 216 and 217:
PP-I-3UTILIZATION OF TAFT EQUATION:
Page 218 and 219:
PP-I-4SELECTIVE HYDROGENATION OF CI
Page 220 and 221:
PP-I-5NON OXIDATIVE REGENERATION ME
Page 222 and 223:
PP-I-6Table 1. Parameters in kineti
Page 224 and 225:
PP-I-7where: k nc , k 1 , k a , k b
Page 226 and 227:
PP-I-8After each adsorption or deso
Page 228 and 229:
PP-I-9The increase in pressure, in
Page 230 and 231:
PP-I-10The analysis of the composit
Page 232 and 233:
PP-I-11The network of βP oxidation
Page 234 and 235:
PP-I-12order of magnitude lower. Th
Page 236 and 237:
PP-I-13ab1,01,0Isotope fraction0,5[
Page 238 and 239:
PP-I-14Relations ‘rate vs alcohol
Page 240 and 241:
PP-I-15[EEAA] t , M[EEAA] t -1 , M
Page 242 and 243:
PP-I-17NEW OSCILLATING REACTION:CAR
Page 244 and 245:
PP-I-18NEW OSCILLATING REACTIONS OF
Page 246 and 247:
PP-I-19KINETICS OF GAS-LIQUID PROCE
Page 248 and 249:
PP-I-20COMPLETE OXIDATION OF HARMFU
Page 250 and 251:
PP-I-21THEORETICAL RESEARCH OF SURF
Page 252 and 253:
PP-I-22INFLUENCE OF ORGANIC HELATES
Page 254 and 255:
PP-I-23The equation of the reaction
Page 256 and 257:
PP-I-25SELECTIVE OXIDATION OF METHA
Page 258 and 259:
PP-I-26coefficients of the equation
Page 260 and 261:
PP-I-27into propionic acid. The giv
Page 262 and 263:
PP-I-28In the studied range of temp
Page 264 and 265:
PP-I-29Table. Reaction temperature
Page 266 and 267:
PP-I-30other in both direction of t
Page 268 and 269:
PP-I-31Reynolds number. The boundar
Page 270 and 271:
PP-I-32NANOPARTICLES AND CATALYSISI
Page 272 and 273:
Section 2.Physico-chemical and math
Page 274 and 275:
PP-II-1For investigation, we used n
Page 276 and 277:
PP-II-2criterion «Zn dissolved in
Page 278 and 279:
PP-II-3exist around the steady stat
Page 280 and 281:
PP-II-4in range 0-1. In our case n
Page 282 and 283:
PP-II-5at comparable activity, the
Page 284 and 285:
PP-II-7CFD-CALCULATION OF MALDISTRI
Page 286 and 287:
PP-II-8INVESTIGATION OF NONLINEAR P
Page 288 and 289:
PP-II-8reactivity. There is a small
Page 290 and 291:
PP-II-10CALCULATION OF INDUSTRIAL C
Page 292 and 293:
PP-II-11type of reactors a catalyst
Page 294 and 295:
PP-II-13MATHEMATTICAL MODELLING OF
Page 296 and 297:
PP-II-13where I Э , M 1Э , M 2Э
Page 298 and 299:
PP-II-14where TOC 0 is the initial
Page 300 and 301:
PP-II-16AUTOCATALYTIC REACTION FRON
Page 302 and 303:
Section 3.Catalytic processesí dev
Page 304 and 305:
PP-III-1for the traditional scheme
Page 306 and 307:
PP-III-2Initial conditions: С i (0
Page 308 and 309:
PP-III-3Afterward, a 30% aqueous hy
Page 310 and 311:
PP-III-4The influence of the water
Page 312 and 313:
PP-III-5Vanadium oxide was grafted
Page 314 and 315:
PP-III-6(T p ) was taken as an inde
Page 316 and 317:
PP-III-7dCdτLABdCNABdτdCdτdCdτd
Page 318 and 319:
PP-III-8O 2 , balanced by He, at a
Page 320 and 321:
PP-III-9Solution of system (3) for
Page 322 and 323:
PP-III-10HDT330ºCHDT350ºCHDT370º
Page 324 and 325:
PP-III-11The activity of Au/support
Page 326 and 327:
PP-III-1249775 m 3 /h0,65Initial te
Page 328 and 329:
PP-III-13through one layer of ACC w
Page 330 and 331:
PP-III-14the runs was always higher
Page 332 and 333:
PP-III-15The experimental data for
Page 334 and 335:
PP-III-16Catalytic hydrogenation of
Page 336 and 337:
PP-III-17The following parameters a
Page 338 and 339:
PP-III-18Figure 1 - Dependence of t
Page 340 and 341:
PP-III-19Our method has some advant
Page 342 and 343:
PP-III-20Furthermore, Ayude et al.
Page 344 and 345:
PP-III-22OPTIMIZATION OF THE METHAN
Page 346 and 347:
PP-III-23EXPERIMENTAL INVESTIGATION
Page 348 and 349:
PP-III-24CATALYTIC REACTORS WITH HY
Page 350 and 351:
PP-III-25ACTIVITY OF Cu/ZSM-5 CATAL
Page 352 and 353:
PP-III-26SIMULATION AND OPTIMISATIO
Page 354 and 355:
PP-III-27model of plug flow reactor
Page 356 and 357:
PP-III-28Calculations were experime
Page 358 and 359:
PP-III-29continuous and pressurized
Page 360 and 361:
PP-III-30adequacy of multistage mod
Page 362 and 363:
PP-III-31+CH 3 OHH 2 O + HO-(CH(CH
Page 364 and 365:
PP-III-32procedure presented by Mar
Page 366 and 367:
PP-III-33HPA-x + 2 H + + Pd 0 ⎯
Page 368 and 369:
PP-III-34of the process as well as
Page 370 and 371:
PP-III-35This study was financially
Page 372 and 373:
PP-III-36phase. Peroxopolyoxometall
Page 374 and 375:
PP-III-37performed under atmospheri
Page 376 and 377:
PP-III-38orders of magnitude larger
Page 378 and 379:
PP-III-39CATALYTIC REACTORS WITH ST
Page 380 and 381:
PP-III-40THE OXIDATIVE DEHYDROGENAT
Page 382 and 383:
PP-III-41MODELLING AND DESIGN OF TH
Page 384 and 385:
PP-III-42COMPLEX TECHNOLOGY OF TREA
Page 386 and 387:
PP-III-43PHOTO ELECTROCHEMISTRY APP
Page 388 and 389:
PP-III-45MODELING OF CATALYTIC α-O
Page 390 and 391:
PP-III-46steady states. It was show
Page 392 and 393:
PP-III-47Results and discussion:The
Page 394 and 395:
PP-III-49FIBROUS PALLADIUM-SUPPORTE
Page 396 and 397:
Section 4.Catalytic technologies in
Page 398 and 399:
PP-IV-1method is adiabatic or autot
Page 400 and 401:
PP-IV-2It had been established that
Page 402 and 403:
PP-IV-4INTERACTION OF ACTIVATED ALU
Page 404 and 405:
PP-IV-5ENVIRONMENTALLY FRIENDLY PRO
Page 406 and 407:
PP-IV-6THE 5%Ni-2%Au/Al 3 CrO 6 SYS
Page 408 and 409:
PP-IV-7MESOPOROUS ANODES BASED ON Y
Page 410 and 411:
PP-IV-8ADVANCED OXIDATION PROCESS F
Page 412 and 413:
PP-IV-9PROCESSING OF POLYMERIC CORD
Page 414 and 415:
PP-IV-10EFFECT OF SULPHUR ON THE CA
Page 416 and 417:
PP-IV-11OXIDATIVE CONVERSION OF MET
Page 418 and 419:
PP-IV-13CATALYTIC FLUE GAS CONDITIO
Page 420 and 421:
PP-IV-14RIBBON POROUS NICKEL BASED
Page 422 and 423:
PP-IV-15ETHANOL CONVERSION TO HYDRO
Page 424 and 425:
PP-IV-16A HIGH-EFFICIENT MICROREACT
Page 426 and 427:
PP-IV-17DIRECT DECOMPOSITION OF NIT
Page 428 and 429:
PP-IV-18NICKEL CATALYSTS BASED ON P
Page 430 and 431:
PP-IV-19SELECTION OF FAVOURABLE FEE
Page 432 and 433:
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
Page 440 and 441:
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
Page 452 and 453: PP-IV-32NEW ELECTRODE MATERIALSFOR
Page 454 and 455: 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 502 and 503: AUTOCLAVE ENGINEERS COMPANYSYSTEMAT
Page 504 and 505: CATACON CATACON CATACON CATACON CAT
Page 510 and 511: George AvgouropoulosFoundation for
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
show all

Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

Create successful ePaper yourself

Delete template?

Save as template?