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PL-2pyrolysis reactor, built in the process after the reactor for upgrading of the primary pyrolysisvapors, or be used to modify the condensed liquids.This contribution is meant to review all opportunities and challenges in headlines, anddiscuss the consequences for process design.References1. Ed. J. Soltes and Thomas A. Milne, Pyrolysis Oils from Biomass, ACS Symposium Series 376, AmericanChemical Society, Washington, DC 1988.9
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 11 and 12: PL-4CATALYTIC CONVERSION OF HYDROCA
Page 13 and 14: PL-4solid oxide fuel cell at direct
Page 15 and 16: PL-5intrinsic kinetics of CH 4 stea
Page 17 and 18: 100 ANNIVERSARY OF PROFESSOR M.I. T
Page 19 and 20: KN-2illustrated by the examples of
Page 21 and 22: CATALYTIC DISTILLATION: PROSPECTS A
Page 23 and 24: KN-5ISOTOPIC TRANSIENT KINETICS STU
Page 25 and 26: CATALYTIC TECHNOLOGIES APPLYING ART
Page 27 and 28: ORAL PRESENTATIONSSection 1. Kineti
Page 29 and 30: KINETICS OF AMMONIA SYNTHESIS AT CA
Page 31 and 32: THE STUDIES OF THE MULTIROUTES MECH
Page 33 and 34: ⎛⎜ kRT ⎜E = ln2F⎜⎜⎝k8
Page 35 and 36: KINETICS OF LIGHT ALKANE OXIDATION:
Page 37 and 38: OP-I-6KINETICS OF STARCH OXIDATION
Page 39 and 40: DESIGN OF CATALYTIC SYSTEMS BASED O
Page 41 and 42: OP-I-8maximum CO 2 formation rate a
Page 43 and 44: OP-I-9This work is a continuation o
Page 45 and 46: OP-I-10the system. In the case of a
Page 47 and 48: OP-I-11(1) [V 5+ O 2- V 5+ ] +CH 4
Page 49 and 50: OP-I-12honeycomb monolith matrices
Page 51 and 52: OP-I-13simulation results. In anoth
Page 53 and 54: OP-I-14T(K)170016001500140013001200
Page 55 and 56: OP-I-15products fraction, the latte
Page 57 and 58: OP-I-16Results and discussionTypica
Page 59 and 60:
OP-I-17The activity measurements we
Page 61 and 62:
OP-I-185 (II-b)6 (III-a)///(K P )H2
Page 63 and 64:
OP-I-19The conversion and selectivi
Page 65 and 66:
OP-I-21DEACTIVATION KINETICS OF PLA
Page 67 and 68:
ON THE DYNAMICS OF NH 3 FORMATIONDU
Page 69 and 70:
OP-I-23STOCHASTIC MODELS FOR THE IM
Page 71 and 72:
OP-I-24NONLINEAR PHENOMENA AND MECH
Page 73 and 74:
OP-I-25EFFECT OF CATALYST FRACTAL D
Page 75 and 76:
Section 2.Physico-chemical and math
Page 77 and 78:
OP-II-2MONTE CARLO SIMULATION OF AD
Page 79 and 80:
OP-II-3IMPROVEMENT OF CALCIUM FLUOR
Page 81 and 82:
OP-II-4DYNAMIC SIMULATION OF A COMP
Page 83 and 84:
MONITORING OF THE PROGRESS OF AN EX
Page 85 and 86:
OP-II-6THE USE OF IONIC LIQUIDS AS
Page 87 and 88:
OP-II-7MULTINUCLEAR NMR IMAGING IN
Page 89 and 90:
OP-II-8MODELING OF DIESEL FILTERS F
Page 91 and 92:
OP-II-9(a) Particle size 100nm (b)F
Page 93 and 94:
OP-III-1CATALYTIC REACTOR FOR N 2 O
Page 95 and 96:
Cu-ZSM5 BASED MONOLITH REACTORS FOR
Page 97 and 98:
NH 3 SCR MODELLING FOR Fe ZEOLITE C
Page 99 and 100:
OP-III-4SCR OF NO x IN DIESEL EXHAU
Page 101 and 102:
OP-III-5CATALYTIC DENSE BIMEVOX MEM
Page 103 and 104:
OP-III-7SIMULATION STUDIES OF A MEM
Page 105 and 106:
OP-III-8MODELLING OF NON-DISPERSIVE
Page 107 and 108:
FRONT VELOCITY AND CRITERION OF TRA
Page 109 and 110:
OP-III-10REACTOR FOR CARBON NANOFIB
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OP-III-11The CCS is also very well
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OP-III-1212342.TS6.TS8.TS12.TS51.TS
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OP-III-13PREPARATION AND PERFORMANC
Page 117 and 118:
OP-III-14MICRO-REACTORS FOR THE COM
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MICROWAVES AND ULTRASOUND TOWARD PR
Page 121 and 122:
OP-III-16FLOW IN THE HONEYCOMB CATA
Page 123 and 124:
OP-III-17HONEYCOMB CATALYSTS WITH P
Page 125 and 126:
OP-III-18METHANE STEAM REFORMING IN
Page 127 and 128:
OP-III-19COMPUTER MODELING OF CATAL
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A REACTOR WITH CO 2 LASER RADIATION
Page 131 and 132:
OP-III-21THE WAY OF METHANOL PRODUC
Page 133 and 134:
OP-III-22MATHEMATICAL MODELLING OF
Page 135 and 136:
OP-III-23NEW ROTOR REACTOR FOR THE
Page 137 and 138:
LOW-TEMPERATURE DIRECT ROUTE TO ANI
Page 139 and 140:
Section 4.Catalytic technologies in
Page 141 and 142:
OP-IV-1low energy efficiency for th
Page 143 and 144:
OP-IV-2which is based on renewable
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OP-IV-3conventional flow reactor, t
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OP-IV-4metal nitrates to yield the
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OP-IV-5Simulation results and concl
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OP-IV-6A home-made copper dispersed
Page 153 and 154:
OP-IV-7desired- and by-products str
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OP-IV-8detectable diffractions of n
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OP-IV-9for the separation of super
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OP-IV-10Exergy analysis:In the pres
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OP-IV-11conditions system; advanced
Page 163 and 164:
OP-IV-12The comparative analysis of
Page 165 and 166:
Results and DiscussionOP-IV-13Table
Page 167 and 168:
OP-V-1DEVELOPMENT OF BIOFUELS PRODU
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HYDRODEOXYGENATION OF FAST-PYROLYSI
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OP-V-3CATALYTIC HYDRODEOXYGENATION
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OP-V-4KINETICS OF CATALYTIC DEOXYGE
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KINETICS OF FFAs ESTERIFICATION:BAT
Page 177 and 178:
OP-V-6TiO 2 /SiO 2 HETEROGENEOUS CA
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OP-V-7CATALYTIC BIOMASS GASIFICATIO
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OP-V-8Rh-PEROVSKITE CATALYSTS FOR B
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OP-V-9AUTOTHERMAL REFORMING OF DIES
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ETHANOL STEAM REFORMING AND WATER G
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IntroductionHYDROGEN PRODUCTION BY
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KINETICS OF THE BIOFUELS-ASSISTED S
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SummaryOP-V-12A gas-phase microreac
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OP-V-13scale monolithic catalysts,
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OP-V-14layer, of 30 μm and 100 μm
Page 197 and 198:
OP-V-15An effect of preliminary RH
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OP-V-16EFFECT OF MICROREACTOR GEOME
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OP-V-17specific heat of combustion
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OP-V-18dynamic saturation with addi
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OP-V-19composition of the gas mixtu
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OP-V-20figure 1. The fluidized bed
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OP-V-21All experiments were conduct
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Section 1.Kinetics of catalytic rea
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PP-I-1conditions of process was hig
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PP-I-2with lateral interaction ener
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PP-I-3We have demonstrated that the
Page 219 and 220:
PP-I-4Organic phase (n-hexane)OOHOH
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PP-I-6KINETICS OF ESTERIFICATION OF
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PP-I-7THE NEW METHOD FOR KINETIC SC
Page 225 and 226:
PP-I-8STOCHASTIC SIMULATION OF ADSO
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STUDY ON CATALYTIC ESTERIFICATION O
Page 229 and 230:
KINETICS OF METHANE OXIDATION OVER
Page 231 and 232:
PP-I-11KINETICS STUDIES AND MECHANI
Page 233 and 234:
PP-I-12MECHANISTIC ASPECTS OF STEAM
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SSITKA IN CONTINUOUS-STIRRED TANK A
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KINETICS OF AN AQUEOUS ALKALI OXIDA
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PP-I-15THE KINETICS OF ACETOACETYC
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KINETIC DECOMPOSITION OF FORMIC ACI
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PP-I-17The preliminary mechanism of
Page 245 and 246:
PP-I-18We have showed that the phen
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PP-I-19diffusion. The plot of the r
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PP-I-20support [17]. The chemical n
Page 251 and 252:
PP-I-21the molecular oxygen is pred
Page 253 and 254:
PP-I-23INVESTIGATION OF METHANOL DE
Page 255 and 256:
PP-I-24NONLINEAR MODELS OF KINETICS
Page 257 and 258:
PP-I-26FIVE-PHASIC OSCILLATORS IN H
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PP-I-27KINETIC REGULARITIES OF N-PR
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KINETICS OF n-BUTANE CONVERSION OVE
Page 263 and 264:
PP-I-29THE CONVERSION OF LIGHT OIL
Page 265 and 266:
KINETICS OF CO OXIDATION OVER Co-ZS
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KINETICS OF SURFACE IRREVERSIBLE RE
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PP-I-31For the first-order reaction
Page 271 and 272:
PP-I-32TableThe calculation of time
Page 273 and 274:
BRØNSTED ACIDITY MEASUREMENT OF FI
Page 275 and 276:
PP-II-2OPTIMIZING OF CHEMICAL REACT
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PP-II-3THERMAL MODES FOR THE CSTR W
Page 279 and 280:
PP-II-4DEACTIVATION OF Rh(410) SURF
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EPR ENLIGHTED PHYSICO-CHEMICAL FUND
Page 283 and 284:
PP-II-6HYDRODYNAMICS OF GAS-SOLID F
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PP-II-71,00,80,60,4Λ=0.01a15100,20
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⎧f⎪⎨f⎪⎩f123( и) k1PCO( 1
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PP-II-9A REACTOR FOR DYNAMIC HIGH P
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PP-II-11TRICKLE-BED CATALYTIC REACT
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PP-II-12INITIAL CONDITIONS OF NON-C
Page 295 and 296:
PP-II-13dMdt− k*315= M⋅ M23⋅
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LIGNOSULPHONATE TOTAL ORGANIC CARBO
Page 299 and 300:
PP-II-15MATHEMATICAL MODELING OF FR
Page 301 and 302:
PP-II-16In this work, we have incre
Page 303 and 304:
VARIANTS OF THE CATALYST BED WITH C
Page 305 and 306:
PP-III-2MATHEMATICAL MODELING OF PE
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PHOTOCATALYTIC SELF CLEANING SURFAC
Page 309 and 310:
PP-III-4OPTIMIZATION AND SCALING UP
Page 311 and 312:
PP-III-5WASHCOATS FOR STRUCTURED RE
Page 313 and 314:
PP-III-6CATALYTIC SELF CLEANING PRO
Page 315 and 316:
PP-III-7ALKYLATION REACTOR MODELING
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PEROVSKITE CATALYSTS FOR NO REDUCTI
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PP-III-9COMPARISON OF IRREVERSIBLE
Page 321 and 322:
PP-III-10SIMULTANEOUS HYDROGENATION
Page 323 and 324:
PP-III-11LOW TEMPERATURE OXIDATION
Page 325 and 326:
PP-III-12IMPROVING THE PROCESS OF H
Page 327 and 328:
POTENTIAL OF WOWEN FIBROUS CATALYTI
Page 329 and 330:
PP-III-14A REACTOR FOR PHOTOELECTRO
Page 331 and 332:
PP-III-15COMPUTER MONITORING OF CAT
Page 333 and 334:
NANOSTRUCTURED POLYMERIC METAL-CONT
Page 335 and 336:
PP-III-17GAS PHASE OXIDATION OF FOR
Page 337 and 338:
PP-III-18DEVELOPMENT OF INDUSTRIAL
Page 339 and 340:
PP-III-19NEW HOMOGENEOUS CATALYTIC
Page 341 and 342:
MODELLING OF PERIODIC OPERATION IN
Page 343 and 344:
REACTOR DESIGN OF THE DIISOBUTYLPHT
Page 345 and 346:
Laboratory experimentsPP-III-22Stud
Page 347 and 348:
PP-III-23Ammonia oxidation process
Page 349 and 350:
PP-III-24analysis and the specific
Page 351 and 352:
PP-III-25Fig. 1 shows the influence
Page 353 and 354:
PP-III-27SIMULATION OF LARGE-SCALE
Page 355 and 356:
DEHYDROGENATION OF С 1 -С 5 PARAF
Page 357 and 358:
PP-III-29A STUDY ON THE ACTIVITY OF
Page 359 and 360:
PP-III-30THE WAY OF METHANOL AND HI
Page 361 and 362:
METHOD FOR PRODUCING OF METHYL LACT
Page 363 and 364:
PP-III-32ON THE ANALYSIS OF PACKED
Page 365 and 366:
PP-III-33PRODUCTION OF METHYLETHYLK
Page 367 and 368:
PP-III-34CLEANING OF CRACK SURFACES
Page 369 and 370:
PP-III-35CATALYTIC OXIDATION OF ORG
Page 371 and 372:
PP-III-36THE ORGANIC COMPOUNDS OXID
Page 373 and 374:
MESOPOROUS CERIA-PRASEODIMIA CATALY
Page 375 and 376:
PP-III-38NON-ARRHENIUS MECHANISMS O
Page 377 and 378:
PP-III-38because of difference of i
Page 379 and 380:
PP-III-39• selective hydrogenatio
Page 381 and 382:
PP-III-40ratio, an increase in the
Page 383 and 384:
PP-III-41rector; v is a volumetric
Page 385 and 386:
PP-III-42achieves 51-100 % at tempe
Page 387 and 388:
PP-III-44MODELING AND OPTIMIZATION
Page 389 and 390:
PP-III-46MATHEMATICAL MODELLING OF
Page 391 and 392:
KINETIC MODELING AND SIMULATION OF
Page 393 and 394:
PP-III-48SIMULATION OF A THREE-STAG
Page 395 and 396:
PP-III-49Activity measurements of s
Page 397 and 398:
PP-IV-1AUTOTHERMAL SORPTION-ENHANCE
Page 399 and 400:
PP-IV-2KINETICS & ECOLOGICAL ASPECT
Page 401 and 402:
PP-IV-3ALUMINUM ACTIVATED BY LIQUID
Page 403 and 404:
PP-IV-4Δ(λ) were measured in a 40
Page 405 and 406:
PP-IV-5depends on the sizes of the
Page 407 and 408:
PP-IV-6activity in POM reaction in
Page 409 and 410:
PP-IV-725 mm diameter and 2 mm thic
Page 411 and 412:
PP-IV-8electrolyte solution is fed
Page 413 and 414:
PP-IV-9formation of large amount of
Page 415 and 416:
PP-IV-10CH 4 /air mixture (with eve
Page 417 and 418:
PP-IV-12LOW-TEMPERATURE REFORMIG OF
Page 419 and 420:
PP-IV-13The new generation of highl
Page 421 and 422:
PP-IV-149585Сonv ersion CH4, %7565
Page 423 and 424:
PP-IV-15carbon containing compounds
Page 425 and 426:
PP-IV-16and MCP3) was 1.6 and 2.4 t
Page 427 and 428:
PP-IV-17Figure 1 shows the dependen
Page 429 and 430:
PP-IV-18contains phases of NiO and
Page 431 and 432:
PP-IV-191. Proportionally less isop
Page 433 and 434:
PP-IV-20amount of parameters: WHSV,
Page 435 and 436:
PP-IV-21on 2%Се/θ-Al 2 O 3 is ca
Page 437 and 438:
PLASMACATALYTIC GAS TREATMENT REACT
Page 439 and 440:
PP-IV-24From the data displayed in
Page 441 and 442:
PP-IV-25process of methane conversi
Page 443 and 444:
PP-IV-26Table 1. Textural, XPS and
Page 445 and 446:
PARTIAL OXIDATION OF METHANE TO C 1
Page 447 and 448:
ResultsPP-IV-29In this work, a homo
Page 449 and 450:
PP-IV-30Fig. 1. Products distributi
Page 451 and 452:
PP-IV-31course of 50 hours of cycli
Page 453 and 454:
PP-IV-32electrodes with mixed oxide
Page 455 and 456:
PP-IV-34PHOTOCATALYTIC WATER SPLITT
Page 457 and 458:
Section 5.Catalytic processing of r
Page 459 and 460:
PP-V-1room temperature for other 48
Page 461 and 462:
PP-V-2CuZnAl < СuZnSi
Page 463 and 464:
PP-V-3half-hydrogenated inter-media
Page 465 and 466:
PP-V-4Results and discussionFig. 1
Page 467 and 468:
REACTORS FOR SYNTHESIS OF LACTIDED.
Page 469 and 470:
PP-V-7METHOD FOR COMPLEX PROCESSING
Page 471 and 472:
PP-V-8THE METHOD FOR PRODUCING OF M
Page 473 and 474:
PP-V-9UPGRADING OF FCC-GASOLINES ON
Page 475 and 476:
PP-V-10TRIGLYCERIDES ALCOHOLYSIS CA
Page 477 and 478:
BIOETHANOL CONVERSION ON ZEOLITE CA
Page 479 and 480:
PP-V-12PRODUCTION OF METHYL FORMATE
Page 481 and 482:
PP-V-13INVESTIGATION OF HYDRODEAROM
Page 483 and 484:
PP-V-14SIMULATION OF TRANSESTERIFIC
Page 485 and 486:
THE KINETICS OF METHANOL STEAM REFO
Page 487 and 488:
PP-V-16SYNGAS PRODUCTION BY PARTIAL
Page 489 and 490:
PP-V-17DEHYDROGENATION/DEHYDRATION
Page 491 and 492:
PP-V-18patterns were recorded in a
Page 493 and 494:
PP-V-19leads to further lowing of C
Page 495 and 496:
Results and DiscussionPP-V-20In Fig
Page 497 and 498:
PP-V-21the hydroxyl group (with pro
Page 499 and 500:
PP-V-23ONE-STAGE PRODUCTION OF HIGH
Page 501 and 502:
ADVERTISEMENT
Page 503 and 504:
AUTOCLAVE ENGINEERS COMPANYUsually
Page 505 and 506:
CATACON CATACON CATACON CATACON CAT
Page 507 and 508:
ÐÅÀÊÒÎÐÑÁÐÎÑ ÂÎÇÄÓ
Page 509 and 510:
LIST OF PARTICIPANTSSadiq AhmedNige
Page 511 and 512:
Katarzyna BawolakTechnical Universi
Page 513 and 514:
Martino Di SerioDepartment of Chemi
Page 515 and 516:
Irene GlikinaVladimir Dal Eastern-U
Page 517 and 518:
Eugene IvanovBoreskov Institute of
Page 519 and 520:
Sareya KozlovaMendeleev University
Page 521 and 522:
Anna LysovaInternational Tomography
Page 523 and 524:
Alexander MyshlyavtsevOmsk Technica
Page 525 and 526:
Joan PapavasiliouFoundation for Res
Page 527 and 528:
Rachid SahkiUniversity Mouloud Mamm
Page 529 and 530:
Olga SimakovaBoreskov Institute of
Page 531 and 532:
Pasi TolvanenÅbo Akademi Universit
Page 533 and 534:
Elena YudinaBoreskov Institute of C
Page 535 and 536:
CONTENTPLENARY LECTURES............
Page 537 and 538:
OP-I-10Fefelov V.F., Gorbunov V.A.,
Page 539 and 540:
OP-II-6Gorri D., Ruiz A., Ortiz A.,
Page 541 and 542:
OP-III-20Mischenko T.I., Snytnikov
Page 543 and 544:
OP-V-2Wildschut J., Heeres H.HYDROD
Page 545 and 546:
PP-I-2Brizhanskaja Ju.A., Brizhansk
Page 547 and 548:
PP-I-29PP-I-30PP-I-31PP-I-32Velichk
Page 549 and 550:
PP-III-5 Essakhi A., Löfberg A., P
Page 551 and 552:
PP-III-29 Palomares A.E., Franch C.
Page 553 and 554:
PP-IV-5 Torosyan G.H., Danial I., A
Page 555 and 556:
PP-IV-30 Solov'ev E.A., Kuvshinov D
Page 557 and 558:
PP-V-23 Rubanov A.E., Kikhtyanin O.
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