OP-II-3

More documents

Recommendations

Info

OP-I-9oxidised and reduced sites, and θx and θy are lump adsorbed hydrocarbon species[3] that either remained adsorbed or go to complete oxidation, depending ontemperature conditions, and only reaction (9) is reversible. One of the mainobjections with respect to the kinetics published so far [5, 6] is that the production ofMA and the accumulation of adsorbed species are not described. The proposedmodel accounts for MA formation and the adsorbed lumped species. Figure 1 showsmodel prediction of temperature and composition from the CSTR for different ratiosof catalyst mass for a constant flow of air at different temperatures. The kineticparameters obtained from the CSTR simulations are tunned to predict observedtemperature profiles from a 2.6 m length and 2.54 cm in diameter fixed-bed reactorpacked with 0.82 mm spheres of externally deposited V 2 O 5 /TiO 2 catalyst [7]operating at typical industrial conditions, and this comparison is shown in figure 2. Animportant aspect of this prediction can be observed in terms of the wide of thepredicted temperature profile wich is comparable in magnitude to the observed one,contrary to most predictions. The corresponding concentration profiles in the reactorfor OX and PA and those for oxidized, reduced and lump adsorbe species are shownin figures 3 and 4. It has been observed that the temperature and compositionprofiles change with time (as shown in figure 5) due to slow but gradualaccummulation of adsorbed species and to reversible deactivation, which can bepartially removed with air in the absence of reaction [7]; this can also be predictedwith the proposed kinetic model, as shown in figure 6, when using kinetic parametersthat described a rather very rapid accumulation of adsorbed species. To be able toadequately describe the moving temperature and reaction fronts in the fixed bedreactor model, the methods of orthogonal collocation (radial) and orthogonalcollocation on finite elements (axial) were used together with a 4th order Runge-Kuttamethod. Four interior collocation points were used in the radial coordinate and 40elements in the axial coordinate with 4 interior points for each element.References[1]. Mars P. & D.W. van Krevelen: Chem. Eng. Sci. Suppl. (1954) 3, 41-59.[2]. Vannice M.A. Catalysis Today (2007) 123, 18-22.[3]. Haber J., R. Tokarz & M. Witko: in New Developments in Selective Oxidation II. Cortés Corberán& Vie Bellón Editors (1994).[4]. Dias C.R., M.F. Portela & G. Bond: Journal of Catalysis (1996)164, 267-287.[5]. Calderbank P.H. et al.: Chem. Eng. Sci. (1977) 32, 1435-1443.[6]. Skrzypek J. et al.: Chem. Eng. Sci. (1985) 40, 611-620.[7]. F. Lopez-Isunza, PhD Thesis, Imperial College, London UK (1983).54
OP-I-9500Flow of Air = 0.3 m 3 (STP)/sec1500Temperature ( o C)450400PATw3= 440 o CTw2= 420 o CTw1= 380 o CTsTgMA0.80.60.40.2Dimensionless Concentration (Cn/C AO)Temperature ( o C)450400ExperimentCalculated350OX 00 10 20 30 40 50 60 70Wcat (gr)Figure 1. Calculations from the CSTR3500 50 100 150 200 250Axial Length (m)Figure 2. Comparison of temperature profilesDimensionles Concentration (Cn/Cao)10.80.60.40.2PAOX00 50 100 150 200 250Axial Length (m)Figure 3. Predicted concentration profilesFraction of Sites (Qo, Qr, Qx)0.80.70.60.50.40.30.20.1QyQoQrQx000 50 100 150 200 250Axial Length (m)0.00150.0010.0005Figure 4. Predicted concentration offraction sitesFraction of Sites QyTemperature ( o C)500450400350Industrial Reactort=06 h12 h16.519 h21 h23 h25 h30 h35 h38.5 hNo ReaccTemperature ( o C)500450400350TS1Ts2Ts3Ts4Ts5Ts6Ts73003000 50 100 150 200Axial Length (m)Figure 5. Evolucion of temperature profilesin the industrial reactor after 38.5 h ofcontinuous operation0 50 100 150 200 250Axial Length (m)Figure 6. Predicted evolucion of temperatureprofiles in the reactor55
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: OP-I-9A REDOX KINETICS FOR THE PART
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 and 596:
PP-III-82Pic. 1 Pic. 2Pic. 1. Schem
Page 597 and 598:
ARKHIPOV Vladimir AfanasievichResea
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

Create successful ePaper yourself

Delete template?

Save as template?