OP-II-3

More documents

Recommendations

Info

ABIEV RufatSt. Petersburg State Institute of Technology(Technical University)Moskowskii pr., 26190013 St. PetersburgRussiaTel: +7 812 494 9276E-mail: rufat.abiev@gmail.comAFANASENKO Vitaliy GennadyevichUfa State Petroleum Technical UniversityKosmonavtov str., 1450062 UfaRussiaE-mail: awirus@rambler.ruAGIRRE IonFaculty of Engineering of Bilbao(University of the Basque Country)Alameda Urquijo s/n48013 BilbaoSpainE-mail: ion.agirre@ehu.esAIOUACHE FaridQueen's University BelfastBT9 5AG BelfastUKE-mail: f.aiouache@qub.ac.ukALEKSEENKO Sergey VladimirovichInstitute of Thermophysics SB RASNovosibirskRussiaE-mail: aleks@itp.nsc.ruALTSHULER Heinrich NaumovichKemerovo Department of the Institute ofSolid State Chemistry andMechanochemistry SB RAS18, Sovetskii ave.650099 KemerovoRussiaTel: +7 384 2 36 3766Fax: +7 384 2 21 1838E-mail: sorbent@kemnet.ruAMARA MouradUniversité des Sciences et de la TechnologieHouari-boumedienneBP 32 El-Alia, Bab-Ezzouar16111 AlgiersAlgeriaTel: +213 21 24-7311Fax: +213 21 24 7311E-mail: mo_amara@yahoo.frLIST OF PARTICIPANTSAMINOVA GuzelKazan State Technological Universityul. Karla Marksa, 68420015 KazanRussiaTel: +7 843 23 14 292Fax: +7 843 23 14 211E-mail: a_guzel@mail.ruAMROUSSE RachidUniversity of PoitiersCNRS 6503 40 Avenue du Recteur Pineau F -86022 POITIERS CedexFranceE-mail: rachid.amrousse@univ-poitiers.frAMUTIO MaiderUniversidad del País Vasco48013 BilbaoSpainE-mail: maider.amutio@ehu.esANFIMOVA Natalya PetrovnaBoreskov Institute of Catalysis SB RASpr. Akademika Lavrentieva, 5630090 NovosibirskRussiaFax: +7 383 330 8056E-mail: anf@catalysis.ruANTAL Steven PeterInterphase Dynamics33 Rosemere12109 TroyUSATel: (518) 395 6985Fax: (518) 833 0219E-mail: antals@rpi.eduARABIOURRUTIA MiriamUniversidad del País Vasco480080 BilbaoSpainE-mail: miriam.arabiourrutia@ehu.esARACIL JoseUniversity of Complutense28040 MadridSpainE-mail: jam1@quim.ucm.esARJMAND MehdiRoyal Institute of Technology (KTH)Valhallavägen, 79SE-100 44 StockholmSwedenTel: +46 8 7906000Fax: +46 8 7906500E-mail: mehdiarjmand@yahoo.com596
ARKHIPOV Vladimir AfanasievichResearch Institute of Applied Mathematicsand Mechanics of Tomsk State UniversityLenina str., 36634050 TomskRussiaTel: +7 3822 529 547Fax: +7 3822 529 547E-mail: leva@niipmm.tsu.ruARPORNWICHAN<strong>OP</strong> AmornchaiChulalongkorn University10330 BangkokThailandE-mail: amornchai.a@chula.ac.thARUTYUNOV Vladimir SergeevichSemenov Institute of Chemical Physics RASKosygina str., 4119991 MoscowRussiaE-mail: arutyunov@center.chph.ras.ruAUTHAYANUN SuthidaChulalongkorn University10330 BangkokThailandE-mail: suthida_autt@hotmail.comAVETISOV Alexander KonstantinovichKarpov Institute of Physical ChemistryVorontsovo pole, 10105064 MoscowRussiaE-mail: avetisov@cc.nifhi.ac.ruAVGOUR<strong>OP</strong>OULOS GeorgeFoundation for Research and Technology-Hellas (FORTH),Institute of Chemical Engineering &High Temperature Chemical Processes(ICE-HT)P.O. Box: 1414, Stadiou Str., Platani-RioGR-26504 PatrasGreeceE-mail: geoavg@iceht.forth.grAVVAKUMOV Evgeny GrigorievichInstitute of Solid State Chemistry andMechanochemistry SB RASKutateladze str., 18630128 NovosibirskRussiaTel: +7 383 332 86 83Fax: +7383 332 28 47E-mail: avvakumov@solid.nsc.ruBABKIN Viatcheslav StepanovichInstitute of Chemical Kinetics andCombustion of SB RASInstitutskaya str., 3630090 NovosibirskRussiaTel: +7(383) 330 91 50Fax: +7(383) 330 73 50E-mail: babkin@kinetics.nsc.ruBACHURIKHIN Alexander LeonidovichN.D. Zelinsky Institute of OrganicChemistry RAS119991 MoscowRussiaE-mail: Shao-kahn@yandex.ruBANKOVIĆ PredragInstitute of Chemistry Technology andMetallurgy, Department of Catalysis andChemical EngineeringNjegoševa, 1211000 BelgradeSerbiaE-mail: predragb@nanosys.ihtm.bg.ac.rsBARAJAS Solano Andrés FernandoIndustrial University of SantanderCiudad Universitaria, Cra 27 calle 9AA678 BucaramangaColombiaTel: +57 7 634 4000Fax: +57 7 645 4697E-mail: andresfdobarajas@gmail.comBARCLAY DonaldAutoclave Engineers Division,Division of Snap-Tite Inc.8325 Hessinger Drive16509 CarnoustieUKTel: +1 814 869 5700Fax: +1 814 860 5811E-mail: donald_barclay@snap-tite.comBARRIO V. LauraUniversity of the Basque Country48013 BilbaoSpainE-mail: laura.barrio@ehu.esBASOV Nikolay LukichA.V. Topchiev Institute of PetrochemicalSynthesis RASLeninskiy pr., 29119991 MoscowRussiaTel: +7 (495) 954 4222Fax: +7 (495) 633 8520E-mail: basov@ips.ac.ruBAWOLAK KatarzynaTechnical University of Lodzul. Zeromskiego 11690-924 LodzPolandE-mail: kbawolak@p.lodz.plBEKSAEV SergeyNordbiochem Ltd.Kuuse 263303 PolvaEstoniaE-mail: sbeksaev@inbox.ru597
Page 1 and 2:
Boreskov Institute of Catalysisof t
Page 3 and 4:
INTERNATIONAL SCIENTIFIC COMMITTEEV
Page 5 and 6:
SILVER SPONSORThe organizers expres
Page 7 and 8:
PL-1HOW TO DESIGN OPTIMAL CATALYTIC
Page 9 and 10:
MULTIFUNCTIONAL DEVICES FOR INTENSI
Page 11 and 12:
PL-3DESIGN OF CATALYTIC PROCESSES F
Page 13 and 14:
PL-3Indeed preparation and testing
Page 15 and 16:
PL-4The second part of the lecture
Page 17 and 18:
PL-5Reactor designs with intensifie
Page 19 and 20:
PL-6MEMBRANE REACTORS: STATE OF THE
Page 21 and 22:
KEY-NOTE PRESENTATIONS
Page 23 and 24:
KN-1description, that can be charac
Page 25 and 26:
KN-2selective catalytic reduction o
Page 27 and 28:
KN-3Fig. 1. Experimental burner of
Page 29 and 30:
KN-4~200°C. This is based on the H
Page 31 and 32:
KN-5for addressing the quality of t
Page 33 and 34:
KN-6reaction with ethanol and the b
Page 35 and 36:
KN-7at temperature lower than 873K,
Page 37 and 38:
REACTION KINETICS AND REACTION ENHA
Page 39 and 40:
OP-I-2RELATION BETWEEN THE ACTIVATI
Page 41 and 42:
COMPARISON OF CHEMICAL AND ENZYMATI
Page 43 and 44:
OP-I-4NONLINEAR PHENOMENA DURING ME
Page 45 and 46:
OP-I-5SPECIFICITY OF THE OSCILLATIO
Page 47 and 48:
OP-I-6TRENDS IN BISTABILITY DOMAINS
Page 49 and 50:
OP-I-7NON-STEADY-STATE CATALYST CHA
Page 51 and 52:
OP-I-8TRANSIENT KINETIC STUDIES OF
Page 53 and 54:
OP-I-9A REDOX KINETICS FOR THE PART
Page 55 and 56:
OP-I-9500Flow of Air = 0.3 m 3 (STP
Page 57 and 58:
OP-I-11ELUCIDATION OF THE REACTIVIT
Page 59 and 60:
KINETIC MODELLING OF THE JOINT TRAN
Page 61 and 62:
OP-I-13n-HEXANE SKELETAL ISOMERIZAT
Page 63 and 64:
OP-I-14the slow branch of kinetic c
Page 65 and 66:
OP-I-15The hydride palladium comple
Page 67 and 68:
Energy Conservation (field j)∂∂
Page 69 and 70:
OP-I-17Selectivity (mol. %)10099989
Page 71 and 72:
OP-I-18According to GLC the main pr
Page 73 and 74:
OP-I-19and slug dimensions, formati
Page 75 and 76:
OP-I-20A RANS volume of fluids [1]
Page 77 and 78:
OP-I-21the physical-chemical charac
Page 79 and 80:
OP-I-22calculated values of pressur
Page 81 and 82:
OP-I-23where L c - capillary length
Page 83 and 84:
OP-I-24and diffuse transmission thr
Page 85 and 86:
OP-I-25effect of bubble break-up wo
Page 87 and 88:
OP-I-26strong influence on the soli
Page 89 and 90:
OP-I-27wHCOOH=1+K2K1(1 + K3⋅ P⋅
Page 91 and 92:
OP-I-28dimensional profiles detecte
Page 93 and 94:
OP-I-29results. The results of the
Page 95 and 96:
OP-I-30Fig. 1. Hydrodynamics and co
Page 97 and 98:
OP-I-31Convection and diffusion wit
Page 99 and 100:
TEMPERATURE RISE DURING REGENERATIO
Page 101 and 102:
OP-II-2[4]. Similar temperature pro
Page 103 and 104:
OP-II-3(Fig, 1 a, b) upon testing i
Page 105 and 106:
OP-II-4In the second step optimizat
Page 107 and 108:
OP-II-5membrane contactors were stu
Page 109 and 110:
OP-II-6reaction over Cu/CeO 2-x cat
Page 111 and 112:
OP-II-7is modelled by means of a tw
Page 113 and 114:
OP-II-8the reactor [6]. However, th
Page 115 and 116:
OP-II-9Figure 1. Computed volume fr
Page 117 and 118:
OP-II-10assumes variables’ distri
Page 119 and 120:
OP-II-11oxide support, it comes tha
Page 121 and 122:
OP-II-12was connected to G.C. via s
Page 123 and 124:
OP-II-13catalyst bed was 6 mm. Thre
Page 125 and 126:
OP-II-14as coolant is an important
Page 127 and 128:
OP-II-15Flow (L/h)7654321Bottoms ra
Page 129 and 130:
OP-II-16(4) The gas recirculation r
Page 131 and 132:
OP-II-17Catalytic reactions were ca
Page 133 and 134:
OP-II-18At steady surface coverage
Page 135 and 136:
OP-II-19gaimpulsegeneratorwateFig.
Page 137 and 138:
OP-II-20examined (see Figure 1). Th
Page 139 and 140:
OP-II-21References[1]. M.P. Dudukov
Page 141 and 142:
OP-II-22of the hydrogen oxidation a
Page 143 and 144:
OP-II-23TemperaturesensorsThe efflu
Page 145 and 146:
OP-II-24of reactant conversions. Pa
Page 147 and 148:
OP-II-25(surface) ‘wall-reaction
Page 149 and 150:
OP-II-26It was found that the 10 wt
Page 151 and 152:
OP-II-27non-flow type. During the M
Page 153 and 154:
OP-III-A-1A NEW SIMPLE MICROCHANNEL
Page 155 and 156:
BUBBLING FLUIDISED BED PYROLYSIS OF
Page 157 and 158:
PINEWOOD PYROLYSIS UNDER VACUUM CON
Page 159 and 160:
OP-III-A-5PYROLYSIS OF HDPE IN A CO
Page 161 and 162:
OP-III-A-6REACTORS FOR THE GREEN TR
Page 163 and 164:
DEHYDRATION OF GLYCEROL TO ACROLEIN
Page 165 and 166:
OP-III-A-8LACTIC ACID BASED ON BIO
Page 167 and 168:
RECOVERY OF ACETIC ACID FROM PYROLY
Page 169 and 170:
OP-III-A-10LIPASE-CATALYZED REACTIO
Page 171 and 172:
OP-III-A-11INVESTIGATION ON THERMOC
Page 173 and 174:
OP-III-A-12SELECTIVE CATALYTIC DEOX
Page 175 and 176:
ETHANOL STEAM REFORMING OVER COBALT
Page 177 and 178:
OP-III-A-14HYDROTREATMENT CATALYSTS
Page 179 and 180:
ORAL PRESENTATIONSSECTION IIIChemic
Page 181 and 182:
OP-III-B-1Reactor parameters:Intern
Page 183 and 184:
OP-III-B-2JOINT STEAM REFORMING OF
Page 185 and 186:
OP-III-B-3LANDFILL BIOGAS PURIFICAT
Page 187 and 188:
OP-III-B-4MODELING AND SIMULATION O
Page 189 and 190:
OP-III-B-5DemonstratorThe medium-te
Page 191 and 192:
OP-III-B-630/19.6 Nl/min (space vel
Page 193 and 194:
OP-III-B-7mixed in the ratios: 94,8
Page 195 and 196:
OP-III-B-8Table 1.Material balance
Page 197 and 198:
OP-III-B-9Based on the results of t
Page 199 and 200:
OP-III-B-10On this basis it can be
Page 201 and 202:
OP-III-B-11Similar trends caused by
Page 203 and 204:
OP-III-B-12(mol/s g cat)x108r4,6-DM
Page 205 and 206:
OP-III-B-13carbon in Wyoming coal i
Page 207 and 208:
OP-III-B-14MODELING PRODUCT DISTRIB
Page 209 and 210:
OP-III-B-15COMBINED TECHNOLOGY OF U
Page 211 and 212:
MATEMATICAL MODEL FOR DOWNDRAFT BIO
Page 213 and 214:
OP-III-B-17CATALYTIC DEHYDRATION OF
Page 215 and 216:
OP-III-B-18SYNGAS AND HYDROGEN PROD
Page 217 and 218:
POSTER PRESENTATIONSSECTION I
Page 219 and 220:
PP-I-1influence of the direction of
Page 221 and 222:
PP-I-2At the agitation of the liqui
Page 223 and 224:
PP-I-3NOLINEAR PHENOMENA IN CATALYT
Page 225 and 226:
PP-I-4A NEW APPROACH TO KINETIC STU
Page 227 and 228:
PP-I-5KINETICS OF PROX REACTION OVE
Page 229 and 230:
PP-I-6PHENOMENA OF SUPERADIABATIC T
Page 231 and 232:
ELECTROMAGNETIC REACTOR OF WATER TR
Page 233 and 234:
PP-I-8DIRECT SYNTHESIS OF HYDROGEN
Page 235 and 236:
PP-I-9DYNAMICS OF FIRST-ORDER PHASE
Page 237 and 238:
PP-I-10ELECTROCHEMICAL OXIDATION OF
Page 239 and 240:
PP-I-11CHEMPAK SOFTWARE PACKAGE: OP
Page 241 and 242:
PP-I-12COMPUTER SIMULATION OF ENDOT
Page 243 and 244:
PP-I-13MODELLING KINETICS OF PROCES
Page 245 and 246:
PP-I-14THE INVESTIGATION OF REACTIO
Page 247 and 248:
PP-I-15The qualitative picture of s
Page 249 and 250:
Thus, knowing the composition of ra
Page 251 and 252:
PP-I-17current density. Preliminary
Page 253 and 254:
PP-I-18Hydrogenation kinetics was d
Page 255 and 256:
PP-I-19the active mixing, amplitude
Page 257 and 258:
PP-I-20where r, h indicate the radi
Page 259 and 260:
PP-I-21model is very anisotropic be
Page 261 and 262:
PP-I-22- Reduction of the number of
Page 263 and 264:
PP-I-23oscillations of intermediate
Page 265 and 266:
PP-I-25SYNTHESIS OF ETHYLENE OXIDE
Page 267 and 268:
PP-I-26OPTIMUM KINETICS FOR POLYSTY
Page 269 and 270:
PP-I-27TableSpecific surface area (
Page 271 and 272:
PP-I-28γ-preirradiated sample), th
Page 273 and 274:
PP-I-29commercial CFD solver FLUENT
Page 275 and 276:
PP-I-30modulus, a considerable decr
Page 277 and 278:
PP-I-31The destruction ways of CF 3
Page 279 and 280:
PP-I-32[7]. Karoor S, Sirkar K. Gas
Page 281 and 282:
PP-I-33above 750°. The catalytic p
Page 283 and 284:
PP-I-35REVERSE FLOW REACTOR WITH FO
Page 285 and 286:
FLOW-RECIRCULATION METHOD FOR INVES
Page 287 and 288:
TO A PROBLEM OF OPTIMIZATION OF FUN
Page 289 and 290:
PP-I-38THE INFLUENCE OF REACTION MI
Page 291 and 292:
PP-I-39METHANOL OXIDATIVE STEAM REF
Page 293 and 294:
PP-I-41CORRECT INVESTIGATION OF THE
Page 295 and 296:
PP-I-42NEW APPROACH OF DEFINITION O
Page 297 and 298:
PP-I-43STREAM HEAT EXCHANGE OF AERO
Page 299 and 300:
PP-I-44HIGH TEMPERATURE OXYGEN TRAN
Page 301 and 302:
PP-I-45KINETICS OF TRANSESTERIFICAT
Page 303 and 304:
MATHEMATICAL MODELING AND OPTIMIZAT
Page 305 and 306:
PP-I-47The basic side reaction is r
Page 307 and 308:
PP-I-49EXPERIMENTAL STUDY OF THE HA
Page 309 and 310:
PP-I-51ON THE KINETICS AND REGULARI
Page 311 and 312:
PP-I-52DIFFERENTIAL THERMAL ANALYSI
Page 313 and 314:
PP-I-53oxidation reaction demonstra
Page 315 and 316:
PP-I-54of reaction. It is establish
Page 317 and 318:
PP-I-55effects, are energetically c
Page 319 and 320:
PP-I-56The experiments and simulati
Page 321 and 322:
PP-I-57In the studied range of temp
Page 323 and 324:
PP-I-58HeadingsAdvances in Chemical
Page 325 and 326:
PP-I-59calculated. During the aroma
Page 327 and 328:
PP-I-60with honeycomb catalyst) act
Page 329 and 330:
Т - temperature, K, D eff - effect
Page 331 and 332:
PP-I-62stirring rate were adopted u
Page 333 and 334:
PP-I-63m 2 = (k 1 y 0 1 +k -1 +k 1
Page 335 and 336:
POSTER PRESENTATIONSSECTION II
Page 337 and 338:
PP-II-1values of operating paramete
Page 339 and 340:
⎡⎛⎢⎜bF⎣⎝=2ab ⎞ 6+ ⎟
Page 341 and 342:
PP-II-4HONEYCOMB MONOLITHIC CATALYS
Page 343 and 344:
MATHEMATICAL MODELING OF THE ALUMIN
Page 345 and 346:
PP-II-6MODELING OF VINYL ACETATE SY
Page 347 and 348:
PP-II-7СENTRIFUGAL DISK REACTORAvv
Page 349 and 350:
PP-II-83) An opportunity of operati
Page 351 and 352:
PP-II-10UV-ACTIVATION OF METHANE CO
Page 353 and 354:
PP-II-11COMBINED APPROACH (FMEA- HA
Page 355 and 356:
PP-II-12Testing the pilot variant o
Page 357 and 358:
PP-II-14NOVEL MICROREACTOR FOR THE
Page 359 and 360:
PP-II-15of 1-2.5 lead to a decreasi
Page 361 and 362:
PP-II-16stages. Kinetic parameters
Page 363 and 364:
PP-II-17whiskers, which assure an a
Page 365 and 366:
PP-II-18с m , с cat - density of
Page 367 and 368:
PP-II-19decrease. So, the potential
Page 369 and 370:
PP-II-20products became a mixture o
Page 371 and 372:
PP-II-21A numerical algorithm and s
Page 373 and 374:
PP-II-22motions at any external con
Page 375 and 376:
PP-II-23One of the main technologic
Page 377 and 378:
PP-II-24100 m x 250 μm x 0.5 μm,
Page 379 and 380:
PP-II-25A model was developed to ca
Page 381 and 382:
PP-II-26The results of calculations
Page 383 and 384:
PP-II-27modes of reaction and two d
Page 385 and 386:
PP-II-29OZONE-DESTRUCTION REACTOR B
Page 387 and 388:
PP-II-30Fig. 1. Axial profile of me
Page 389 and 390:
PP-II-31isobutylene in butene fract
Page 391 and 392:
PP-II-322.5x10 -3 ( i )2.5x10 -3 (
Page 393 and 394:
PP-II-33No olefinreadsorptionWith o
Page 395 and 396:
PP-II-34using titania or Ag-doped t
Page 397 and 398:
PP-II-35accidents, is condition dep
Page 399 and 400:
PP-II-36be seen that at temperature
Page 401 and 402:
PP-II-37the solid phase solute conc
Page 403 and 404:
PP-II-38As shown in Table 1, the ca
Page 405 and 406:
PP-II-39better to the obtained in t
Page 407 and 408:
PP-II-40Hydrodynamic regime in the
Page 409 and 410:
PP-II-41activity, relative unit1,21
Page 411 and 412:
PP-II-42One of the major indicators
Page 413 and 414:
PP-II-43These conditions are confor
Page 415 and 416:
PP-II-44For the hepten, alpha-methy
Page 417 and 418:
PP-II-46PARTIAL OXIDATION OF METHAN
Page 419 and 420:
PP-II-47DEVELOPMENT OF VORTEX APPAR
Page 421 and 422:
MODELING OF CFTALYTIC α-OLEFINS OL
Page 423 and 424:
PP-II-49Hinselwood kinetic equation
Page 425 and 426:
3) iterate concentrations at a cut
Page 427 and 428:
PP-II-51data such flow sheet provid
Page 429 and 430:
PP-II-53ON THE TECNOLOGY OF TECHNIC
Page 431 and 432:
PP-II-54PROPYLENE POLYMERIZATION AN
Page 433 and 434:
REACTOR FOR LIQUID-PHASE PROCESSES
Page 435 and 436:
PP-II-56MODELING OF CATALYTIC MICRO
Page 437 and 438:
PP-II-57MATHEMATICAL MODELING OF BE
Page 439 and 440:
PP-II-58HONEYCOMB CATALYSTS WITH PO
Page 441 and 442:
POSTER PRESENTATIONSSECTION IIISECT
Page 443 and 444:
ReferencesPP-III-1[1]. A.N. Pestrya
Page 445 and 446:
PP-III-2Table1. Percentages of diff
Page 447 and 448:
PP-III-3conversion for the reaction
Page 449 and 450:
PP-III-4900Reformer temperature (K)
Page 451 and 452:
PP-III-5Catalytic performance of th
Page 453 and 454:
PP-III-6optimization permit better
Page 455 and 456:
PP-III-8DE-NO X SYSTEM BASED ON H 2
Page 457 and 458:
PP-III-9SEPARATION BETWEEN CHLORIDE
Page 459 and 460:
CONVERSION OF WASTE COTTON TO BIOET
Page 461 and 462:
PP-III-12THE METHOD OF GLYCERIC ACI
Page 463 and 464:
NOx conversion vs. temperature is p
Page 465 and 466:
PP-III-14intermetallic diffusion at
Page 467 and 468:
PP-III-15The conversion of O 2 was
Page 469 and 470:
PP-III-16H 2consumpition (a.u)(a)39
Page 471 and 472:
PP-III-17the characteristic structu
Page 473 and 474:
PP-III-18Figure 1. Influence of tem
Page 475 and 476:
PP-III-19(a)(b)CH 4conversion, %100
Page 477 and 478:
PP-III-20take into account own size
Page 479 and 480:
PP-III-2110080CS-18CS-34CHZ30CHZ801
Page 481 and 482:
EXPERIMENTALPP-III-22We synthesized
Page 483 and 484:
PP-III-23Base composition component
Page 485 and 486:
PP-III-25CO REMOVAL AT THE MICROSCA
Page 487 and 488:
HYDROGEN PRODUCTION FROM METHANOL U
Page 489 and 490:
PP-III-27NON CATALITIC PRODUCTION O
Page 491 and 492:
PP-III-28Different reaction conditi
Page 493 and 494:
PP-III-29followed by WGS reaction.
Page 495 and 496:
PP-III-30As a solvent-coreactants w
Page 497 and 498:
PP-III-31It was concluded that on t
Page 499 and 500:
PP-III-32Hydrogenolysis of glycerol
Page 501 and 502:
PP-III-331,6W 0, μmol Н 2/min1,20
Page 503 and 504:
PP-III-34preparation (glass fiber f
Page 505 and 506:
PP-III-35In the modification proces
Page 507 and 508:
PP-III-36The kinetics of acid hydro
Page 509 and 510:
PP-III-37reaction: i) C=O double bo
Page 511 and 512:
PP-III-38methane and carbon monoxid
Page 513 and 514:
PP-III-39from 25 to 60, which was d
Page 515 and 516:
PP-III-401% w/w for Pd with respect
Page 517 and 518:
PP-III-41material. Besides, the mol
Page 519 and 520:
PP-III-43METHANOL AND DIMETHYL ETHE
Page 521 and 522:
PP-III-44goal is attained by using
Page 523 and 524:
OLIGOMERISATION OF TERTIARY AMINE L
Page 525 and 526:
PP-III-47meter (Shimazu Co.; TOC-50
Page 527 and 528:
PP-III-48the range of 29-87 kJ/mol
Page 529 and 530:
PP-III-49determine the optimal type
Page 531 and 532:
PP-III-50NEW CONCEPT FOR A SELF CLE
Page 533 and 534:
PP-III-51HYDROGEN PRODUCTION BY MET
Page 535 and 536:
PP-III-52CATALYTIC UPGRADING OF PRO
Page 537 and 538:
PP-III-53CATALYTIC CONVERSION OF FI
Page 539 and 540:
PROCESS FOR THE PRODUCTION OF BUTYL
Page 541 and 542:
PP-III-55been previously fixed and
Page 543 and 544:
PP-III-56The influence of reaction
Page 545 and 546: PP-III-57sample does not contain so
Page 547 and 548: PP-III-58The re-activation of the e
Page 549 and 550: PP-III-59The aim of this work is th
Page 551 and 552: PP-III-61BIODIESEL FROM MICROALGAE
Page 553 and 554: DEVELOPING MICROFLUIDIC DEVICE WITH
Page 555 and 556: THREE-PHASE DIRECT OILS HYDROGENATI
Page 557 and 558: Co-BASED CATALYSTS FOR THE HYDROLYS
Page 559 and 560: PP-III-65KINETIC STUDY OF THE CATAL
Page 561 and 562: PP-III-66PRODUCTION OF HYDROGEN AND
Page 563 and 564: PP-III-67ENHANCED GASIFICATION OF P
Page 565 and 566: PP-III-68INFLUENCE OF SPILLOVER ON
Page 567 and 568: PP-III-69AEROBIC OXIDATIVE COUPLING
Page 569 and 570: PP-III-70MECHANISMS FOR CHEMICAL RE
Page 571 and 572: PP-III-70SBS molecules and increase
Page 573 and 574: PP-III-71and as a resut, could enha
Page 575 and 576: PP-III-72conversion). Al 2 O 3 /PSS
Page 577 and 578: PP-III-73SBA50TiSBA% Transmittance5
Page 579 and 580: PP-III-74stove heating. Another par
Page 581 and 582: PP-III-75TG [%]0-10-20-30380°C400
Page 583 and 584: PP-III-76The elementary version of
Page 585 and 586: PP-III-77thermodynamically enhanced
Page 587 and 588: PP-III-78GFC textileStructuringmeta
Page 589 and 590: PP-III-79All the prepared spinel-ox
Page 591 and 592: PP-III-80Our new process is polluti
Page 593 and 594: PP-III-81Fig. 1. Scheme of the biog
Page 595: PP-III-82Pic. 1 Pic. 2Pic. 1. Schem
Page 599 and 600: CENTENO Felipe OrlandoNúcleo de Ex
Page 601 and 602: FLID Mark RafailovichScientific Res
Page 603 and 604: HOSEN Mohammad AnwarUniversity of M
Page 605 and 606: KOZLOVA EkaterinaBoreskov Institute
Page 607 and 608: MAKARSHIN Lev LvovichBoreskov Insti
Page 609 and 610: ONSAN Zeynep IlsenDepartment of Che
Page 611 and 612: REBOLLAR MoisesInstituto De Investi
Page 613 and 614: SHEIKH Munir AhmedTraining and Staf
Page 615 and 616: SULMAN Esfir MikhailovnaTver Techni
Page 617 and 618: ZHAPBASBYEV Uzak KairbekovichKazakh
Page 619 and 620: OP-I-3 Pécar D., Gorsek A.COMPARIS
Page 621 and 622: OP-II-3Kucherov A.V., Finashina E.D
Page 623 and 624: OP-III-A-9 Rasrendra C.B., Girisuta
Page 625 and 626: PP-I-9Bykov V., Tsybenova S.B.DYNAM
Page 627 and 628: PP-I-43 Pechenegov Y.Y., Kuzmina R.
Page 629 and 630: PP-II-10 Basov N.L., Oreshkin I., T
Page 631 and 632: PP-II-45 Stepanek J., Koci P., Kubi
Page 633 and 634: PP-III-19 Fedorova Z.A., Danilova M
Page 635 and 636: PP-III-53 Pölczmann G., Valyon J.,
Page 637: XIX International Conference on Che
show all

OP-II-3

You also want an ePaper? Increase the reach of your titles

Delete template?

Save as template?