Fluidization engineering:
Gespeichert in:
| Hauptverfasser: | , |
|---|---|
| Format: | Buch |
| Sprache: | English |
| Veröffentlicht: |
Boston u.a.
Butterworth-Heinemann
1991
|
| Ausgabe: | 2. ed. |
| Schriftenreihe: | Butterworth-Heinemann series in chemical engineering
|
| Schlagworte: | |
| Online-Zugang: | Inhaltsverzeichnis |
| Beschreibung: | XXVII, 491 S. graph. Darst. |
Internformat
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| 245 | 1 | 0 | |a Fluidization engineering |c Daizo Kunii ; Octave Levenspiel* |
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Datensatz im Suchindex
| _version_ | 1804118718642388992 |
|---|---|
| adam_text | FLUIDIZATION ENGINEERING SECOND EDITION DAIZO KUNII FUKUI INSTITUTE OF
TECHNOLOGY FUKUI CITY, JAPAN OCTAVE LEVENSPIEL CHEMICAL ENGINEERING
DEPARTMENT OREGON STATE UNIVERSITY CORVALLIS, OREGON
BUTTERWORTH*HEINEMANN BOSTON LONDON SINGAPORE SYDNEY TORONTO WELLINGTON
CONTENTS PREFACE TO THE SECOND EDITION XVII PREFACE TO THE FIRST EDITION
XIX NOTATION XXI CHAPTER 1 INTRODUCTION 1 THE PHENOMENON OF FLUIDIZATION
LIQUIDLIKE BEHAVIOR OF A. FLUIDIZED BED COMPARISON WITH OTHER CONTACTING
METHODS ADVANTAGES AND DISADVANTAGES OF FLUIDIZED BEDS FOR INDUSTRIAL
OPERATIONS FLUIDIZATION QUALITY SELECTION OF A CONTACTING MODE FOR A
GIVEN APPLICATION OVERALL PLAN RELATED READINGS 1 4 7 10 11 11 12 13
CHAPTER2 INDUSTRIAL APPLICATIONS OF FLUIDIZED BEDS 15 HISTORICAL
HIGHLIGHTS 15 COAL GASIFICATION 15 GASOLINE FROM OTHER PETROLEUM
FRACTIONS 15 GASOLINE FROM NATURAL AND SYNTHESIS GASES 17 SYNTHESIS
REACTIONS 18 METALLURGICAL AND OTHER PROCESSES 18 PHYSICAL OPERATIONS 19
HEAT EXCHANGE 19 SOLIDIFICATION OF A MELT TO MAKE GRANULES 20 VIA
CONTENTS CHAPTER 6 COALESCENCE AND SPLITTING OF BUBBLES INTERACTION OF
TWO ADJACENT BUBBLES COALESCENCE, BUBBLE SIZE, AND BUBBLE FREQUENCY
SPLITTING OF BUBBLES AND MAXIMUM BUBBLE SIZE BUBBLE FORMATION ABOVE A
DISTRIBUTOR EXAMPLE 2. INITIAL BUBBLE SIZE AT A DISTRIBUTOR? SLUG FLOW
PROBLEMS REFERENCES BUBBLING FLUIDIZED BEDS EXPERIMENTAL FINDINGS
EMULSION MOVEMENT FOR SMALL (GELDART B) AND FINE (GELDART A) PARTICLES
EMULSION MOVEMENT FOR LARGE (GELDART D) PARTICLES EMULSION GAS FLOW AND
VOIDAGE EFFECT OF PRESSURE ON BED PROPERTIES EFFECT OF TEMPERATURE ON
BED PROPERTIES ESTIMATION OF BED PROPERTIES GAS FLOW IN THE EMULSION
PHASE BUBBLE GAS FLOW BUBBLE SIZE AND BUBBLE GROWTH BUBBLE RISE VELOCITY
BEDS WITH INTERNALS EXAMPLE 1. BUBBLE SIZE AND RISE VELOCITY IN GELDART
A BEDS EXAMPLE 2. BUBBLE SIZE AND RISE VELOCITY IN GELDART B BEDS
PHYSICAL MODELS: SCALE-UP AND SCALE-DOWN EXAMPLE 3. SCALE-DOWN OF A
COMMERCIAL CHLORINATOR FLOW MODELS FOR BUBBLING BEDS GENERAL
INTERRELATIONSHIP AMONG BED PROPERTIES THE SIMPLE TWO-PHASE MODEL THE
K-L MODEL WITH ITS DAVIDSON BUBBLES AND WAKES EXAMPLE 4. REACTOR
SCALE-UP FOR GELDART A CATALYST EXAMPLE 5. REACTOR SCALE-UP FOR GELDART
B CATALYST PROBLEMS REFERENCES 126 126 127 129 130 132 132 134 134 137
137 137 139 141 141 142 143 143 143 144 146 150 150 151 152 153 154 155
155 156 159 161 162 164 CHAPTER 7 ENTRAINMENT AND ELUTRIATION FROM
FLUIDIZED BEDS 165 FREEBOARD BEHAVIOR 165 ORIGIN OF SOLIDS EJECTED INTO
THE FREEBOARD 167 CONTENTS EXPERIMENTAL FINDINGS LOCATION OF THE GAS
OUTLET OF A VESSEL ESTIMATION OF THE TDH ENTRAINMENT FROM TALL VESSELS:
H F TDH PROCEDURE OF ZENZ ET AL. [21,8] THE ELUTRIATION CONSTANT
APPROACH RELATIONSHIP BETWEEN K AND G S EXPERIMENTAL METHODS FOR FINDING
K AND K* EXPERIMENTAL FINDINGS FOR K* EXAMPLE 1. ENTRAINMENT FROM FINE
PARTICLE BEDS WITH HIGH FREEBOARD EXAMPLE 2. ENTRAINMENT FROM LARGE
PARTICLE BEDS WITH HIGH FREEBOARD EXAMPLE 3. ENTRAINMENT FROM BEDS WITH
A WIDE SIZE DISTRIBUTION OF SOLIDS EXAMPLE 4. K* FROM STEADY STATE
EXPERIMENTS EXAMPLE 5. COMPARING PREDICTIONS FOR K * ENTRAINMENT FROM
SHORT VESSELS: IFF TDH FREEBOARD-ENTRAINMENT MODEL EXAMPLE 6.
ENTRAINMENT FROM A SHORT VESSEL: PROBLEMS REFERENCES H F TDH 168 173
173 174 174 175 176 176 177 179 180 181 181 181 183 184 190 190 191
CHAPTER8 HIGH-VELOCITY FLUIDIZATION 193 TURBULENT FLUIDIZED BEDS 193
EXPERIMENTAL FINDINGS 193 FAST FLUIDIZATION 195 EXPERIMENTAL FINDINGS
197 THE FREEBOARD-ENTRAINMENT MODEL APPLIED TO FAST FLUIDIZATION 201
DESIGN CONSIDERATIONS 203 PRESSURE DROP IN TURBULENT AND FAST
FLUIDIZATION 206 EXAMPLE 1. PERFORMANCE OF A FAST FLUIDIZED VESSEL 206
CHAPTER 9 PROBLEMS REFERENCES SOLID MOVEMENT: MIXING, SEGREGATION, AND
STAGING VERTICAL MOVEMENT OF SOLIDS EXPERIMENTAL FINDINGS DISPERSION
MODEL COUNTERFLOW SOLID CIRCULATION MODELS RELATING THE COUNTERFLOW TO
THE DISPERSION MODEL COARSE PARTICLE BEDS EXAMPLE 1. VERTICAL MOVEMENT
OF SOLIDS 209 209 211 212 212 214 215 216 217 218 CONTENTS HORIZONTAL
MOVEMENT OF SOLIDS EXPERIMENTAL FINDINGS MECHANISTIC MODEL BASED ON THE
DAVIDSON BUBBLE EXAMPLE 2. HORIZONTAL DRIFT OF SOLIDS SEGREGATION OF
PARTICLES MIXING-SEGREGATION EQUILIBRIUM STEADY STATE SEPARATION OF
PARTICLES LARGE SOLIDS IN BEDS OF SMALLER PARTICLES LARGE SOLIDS RESTING
ON DISTRIBUTORS STAGING OF FLUIDIZED BEDS BATCH OF SOLIDS THROUGHFLOW OF
SOLIDS LEAKAGE OF SOLIDS THROUGH DISTRIBUTOR PLATES EXAMPLE 3. DESIGN OF
BAFFLE PLATES PROBLEMS REFERENCES 219 219 220 222 223 223 225 226 228
228 228 231 231 232 232 233 CHAPTER 10 GAS DISPERSION AND GAS
INTERCHANGE IN BUBBLING BEDS 237 DISPERSION OF GAS IN BEDS 237 STEADY
STATE TRACER STUDIES 237 STIMULUS-RESPONSE STUDIES 242 GAS INTERCHANGE
BETWEEN BUBBLE AND EMULSION 245 DEFINITIONS OF GAS INTERCHANGE 245
EXPERIMENTAL METHODS 246 EXPERIMENTAL FINDINGS ON INTERCHANGE
COEFFICIENTS 248 ESTIMATION OF GAS INTERCHANGE COEFFICIENTS 250 EXAMPLE
1. ESTIMATE INTERCHANGE COEFFICIENTS IN BUBBLING BEDS . 253 EXAMPLE 2.
COMPARE THE RELATIVE IMPORTANCE OF K BC AND K CE 254 EXAMPLE 3. COMPARE
INTERCHANGE RATES FOR . ADSORBED AND NONADSORBED GASES 255 PROBLEM 255
REFERENCES 256 CHAPTER LL PARTICLE-TO-GAS MASS AND HEAT TRANSFER 257
MASS TRANSFER: EXPERIMENTAL 257 SINGLE SPHERES AND FIXED BEDS 257 . GAS
FLUIDIZED BEDS * 258 INTERPRETATION OF MASS TRANSFER COEFFICIENTS 259
MASS TRANSFER RATE FROM THE BUBBLING BED MODEL 260 EFFECT OF ADSORPTION
ON THE INTERCHANGE COEFFICIENT K D 263 CONTENTS XI EXAMPLE 1. FITTING
REPORTED MASS TRANSFER DATA WITH THE BUBBLING BED MODEL 265 EXAMPLE 2.
THE EFFECT OF M ON BUBBLE-EMULSION INTERCHANGE 267 HEAT TRANSFER:
EXPERIMENTAL 268 SINGLE SPHERES AND FIXED BEDS 268 GAS FLUIDIZED BEDS
268 INTERPRETATION OF HEAT TRANSFER COEFFICIENTS 270 ATTEMPT AT
MEASURING H P DIRECTLY IN FINE PARTICLE BEDS 271 HEAT TRANSFER FROM THE
BUBBLING BED MODEL 271 EXAMPLE 3. FITTING REPORTED HEAT TRANSFER DATA
WITH THE BUBBLING BED MODEL 273 EXAMPLE 4. HEATING A PARTICLE IN A
FLUIDIZED BED 274 PROBLEMS 275 REFERENCES 276 CHAPTER 12 CONVERSION OF
GAS IN CATALYTIC REACTIONS 277 MEASURES OF REACTION RATE AND REACTOR
PERFORMANCE 277 PREVIOUS FINDINGS 278 EXPERIMENTAL INVESTIGATIONS 278
REACTOR MODELS 284 MODELS FOR COMPLEX REACTIONS 285 MULTIPLE STABILITY
286 DESIGN AND SCALE-UP PROCEDURES 288 REACTOR MODEL FOR FINE PARTICLE
BUBBLING BEDS 289 FIRST-ORDER REACTION 290 SPECIAL CASES OF THE
CONVERSION EQUATION 292 CONVERSION EFFICIENCY COMPARED TO PLUG FLOW 293
EXAMPLE 1. FINE PARTICLE (GELDART A) BUBBLING BED REACTOR 293
APPLICATION TO MULTIPLE REACTIONS 294 EXAMPLE 2. COMMERCIAL-SIZED
PHTHALIC ANHYDRIDE REACTOR 298 REACTOR MODEL FOR BUBBLING BEDS OF
INTERMEDIATE-SIZED PARTICLES OR MF /E MF B 5 MF ^M{ 300 EXAMPLE
3. BUBBLING BED REACTOR FOR INTERMEDIATE-SIZED PARTICLES 302 REACTOR
MODEL FOR LARGE PARTICLE BUBBLING BEDS 303 EXAMPLE 4. REACTION IN THE
SLOW BUBBLE REGIME 305 REACTOR MODEL FOR THE FREEBOARD REGION ABOVE
FLUIDIZED BEDS 305 EXAMPLE 5. CONVERSION IN THE FREEBOARD OF A REACTOR
307 TURBULENT BED REACTORS 308 XII CONTENTS FAST FLUIDIZED BED REACTORS
309 PROBLEMS 309 REFERENCES 310 CHAPTER 13 HEAT TRANSFER BETWEEN
FLUIDIZED BEDS AND SURFACES 313 EXPERIMENTAL FINDINGS 313 HEAT TRANSFER
COEFFICIENT 313 VERTICAL TUBES AND BED WALLS 314 HORIZONTAL TUBES 314
SPLASH ZONE 317 TEMPERATURE EFFECT 317 OBJECTS IMMERSED IN BUBBLING BEDS
318 FAST FLUIDIZED AND SOLID CIRCULATION SYSTEMS 320 RADIANT HEAT
TRANSFER 320 HEAT TRANSFER PROPERTIES OF INCIPIENTLY FLUIDIZED BEDS ,
322 HEAT TRANSFER AT A DISTRIBUTOR PLATE 323 THEORETICAL STUDIES 323
FIXED AND INCIPIENTLY FLUIDIZED BEDS 323 BUBBLING BEDS*HEAT TRANSFER TO
EMULSION PACKETS 326 BUBBLING BEDS* H AT A HEAT EXCHANGER SURFACE 328 H
BETWEEN MOVING BEDS AND HEAT EXCHANGE WALLS * 330 FREEBOARD REGION, FAST
FLUIDIZATION, AND CIRCULATING SOLID SYSTEMS 330 EXAMPLE 1. H ON A
HORIZONTAL TUBE BANK 331 EXAMPLE 2. EFFECT OF GAS PROPERTIES ON H 332
EXAMPLE 3. EFFECT OF PARTICLE SIZE ON H 332 EXAMPLE 4. FREEBOARD HEAT
EXCHANGE 334 PROBLEMS 334 REFERENCES 335 CHAPTER 14 THE RTD AND SIZE
DISTRIBUTION OF SOLIDS IN FLUIDIZED BEDS 337 PARTICLES OF UNCHANGING
SIZE 337 FEED OF ONE SIZE, SINGLE AND MULTISTAGE BEDS 337 FEED OF WIDE
SIZE DISTRIBUTION 340 SIMPLE EXTENSIONS 342 EXAMPLE 1. FLOW WITH
ELUTRIATION 343 EXAMPLE 2. FLOW WITH ELUTRIATION AND CHANGE IN DENSITY
OF SOLIDS 344 PARTICLES OF CHANGING SIZE 345 RATE EXPRESSIONS FOR
GROWING AND SHRINKING PARTICLES 345 GENERAL PERFORMANCE EQUATIONS 346
CALCULATION PROCEDURE FOR THE GENERAL SITUATION 347 CONTENTS LINEAR
SHRINKAGE, SINGLE-SIZE FEED, NO ELUTRIATION 349 LINEAR GROWTH,
SINGLE-SIZE FEED, NO ELUTRIATION 350 COMMENTS AND LIMITATIONS 351
EXAMPLE 3. SINGLE-SIZE FEED OF SHRINKING PARTICLES 351 EXAMPLE 4. WIDE
SIZE DISTRIBUTION OF SHRINKING PARTICLES 352 EXAMPLE 5. ELUTRIATION AND
ATTRITION OF CATALYST 353 PROBLEMS 356 REFERENCES 357 CHAPTER 15
CIRCULATION SYSTEMS 359 CIRCUITS FOR THE CIRCULATION OF SOLIDS 359
CLASSIFICATION OF CIRCULATION LOOPS 359 PRESSURE BALANCE IN A
CIRCULATION LOOP 361 FINDING REQUIRED CIRCULATION RATES 365 CIRCULATION
RATE FOR DEACTIVATING CATALYSTS 365 CIRCULATION RATE FOR A REQUIRED HEAT
REMOVAL RATE 367 EXAMPLE 1. CIRCULATION RATE WHEN DEACTIVATION CONTROLS
369 EXAMPLE 2. CIRCULATION RATE WHEN HEAT DUTY CONTROLS 369 FLOW OF
GAS-SOLID MIXTURES IN DOWNCOMERS 371 DOWNWARD DISCHARGE FROM A VERTICAL
PIPE 373 MOVING BED DOWNFLOW 374 FLUIDIZED DOWNFLOW 375 FLUIDIZED
DOWNFLOW IN TALL DOWNCOMERS 376 COMMENTS ON DOWNCOMERS 377 EXAMPLE 3.
AERATION OF A FINE PARTICLE DOWNCOMER 379 EXAMPLE 4. CIRCULATION IN
SIDE-BY-SIDE BEDS 380 EXAMPLE 5. STEAM SEAL OF A COARSE PARTICLE
DOWNCOMER 381 FLOW IN PNEUMATIC TRANSPORT LINES 383 VERTICAL UPFLOW OF
SOLIDS 383 HORIZONTAL FLOW 384 SAFE GAS VELOCITY FOR PNEUMATIC TRANSPORT
385 PRESSURE DROP IN PNEUMATIC TRANSPORT 385 PRESSURE DROP IN BENDS 388
PRACTICAL CONSIDERATIONS 388 PROBLEMS 392 REFERENCES 394 CHAPTER 16
DESIGN FOR PHYSICAL OPERATIONS 397 INFORMATION NEEDED FOR DESIGN 397
HEAT TRANSFER . 398 XIV CONTENTS BATCH OPERATIONS CONTINUOUS OPERATIONS
HEAT LOSS TO SURROUNDINGS EXAMPLE 1. SINGLE-STAGE LIMESTONE CALCINER
EXAMPLE 2. MULTISTAGE LIMESTONE CALCINER MASS TRANSFER BATCH OPERATIONS
CONTINUOUS OPERATIONS EXAMPLE 3. MULTISTAGE ADSORBER DRYING OF SOLIDS
BATCH OPERATIONS CONTINUOUS OPERATIONS EXAMPLE 4. DRYER KINETICS AND
SCALE-UP EXAMPLE 5. SOLVENT RECOVERY FROM POLYMER PARTICLES PROBLEMS
REFERENCES 398 400 403 404 405 408 408 410 413 415 415 418 422 * 423 426
427 CHAPTER 17 DESIGN OF CATALYTIC REACTORS 429 BENCH-SCALE REACTORS 429
PILOT-PLANT REACTORS 430 DESIGN DECISIONS 431 EXAMPLE 1. REACTOR
DEVELOPMENT PROGRAM 434 EXAMPLE 2. DESIGN OF A COMMERCIAL ACRYLONITRILE
REACTOR . 438 DEACTIVATING CATALYSTS 440 EXAMPLE 3. REACTOR-REGENERATOR
WITH CIRCULATING CATALYST: CATALYTIC CRACKING 444 PROBLEMS 447
REFERENCES 448 CHAPTER 18 THE DESIGN OF NONCATALYTIC GAS-SOLID REACTORS
449 KINETIC MODELS FOR THE CONVERSION OF SOLIDS 450 UNIFORM-REACTION
MODEL FOR POROUS SOLIDS OF UNCHANGING SIZE 450 SHRINKING-CORE MODEL
FOR SOLIDS OF UNCHANGING SIZE 451 INTERMEDIATE MODELS FOR PARTICLES OF
UNCHANGING SIZE 453 MODELS FOR SHRINKING PARTICLES 454 FINDING THE
RIGHT MODEL 455 MODELS FOR THE REACTION OF SOLIDS ALONE 456 EXAMPLE 1.
KINETICS OF ZINC BLENDE ROASTING 456 EXAMPLE 2. KINETICS OF CARBON
BURNING 457 CONVERSION OF SOLIDS OF UNCHANGING SIZE 457 SINGLE-SIZE
PARTICLES AND SINGLE.FLUIDIZED BED 457 CONTENTS SINGLE-SIZE PARTICLES
AND MULTIPLE FLUIDIZED BEDS SIZE DISTRIBUTION OF PARTICLES IN A SINGLE
BED REMARKS EXAMPLE 3. ROASTING KINETICS FROM FLOWING SOLIDS DATA
EXAMPLE 4. SCALE-UP OF A REACTOR WITH FLOWING SOLIDS CONVERSION OF
SHRINKING AND GROWING PARTICLES CONVERSION OF BOTH GAS AND SOLIDS
PERFORMANCE CALCULATIONS FOR THE LARGE PARTICLE BED (CASE Z) PERFORMANCE
CALCULATIONS FOR THE FINE PARTICLE BED (CASE W) EXAMPLE 5. DESIGN OF A
ROASTER FOR FINELY _J GROUND ORE EXAMPLE 6. DESIGN OF A ROASTER FOR
COARSE ORE MISCELLANEOUS EXTENSIONS WIDE SIZE DISTRIBUTION OF A BATCH OF
PARTICLES WIDE SIZE DISTRIBUTION OF FEED SOLIDS TO A FLUIDIZED BED
FLUIDIZED COAL COMBUSTION REACTOR-REGENERATOR SYSTEM FOR SOLIDS OF
CHANGING SIZE PROBLEMS REFERENCES 459 460 461 462 462 464 464 466 467
468 471 473 473 473 * 474 476 476 479 AUTHOR INDEX 481 SUBJECT INDEX 487
|
| any_adam_object | 1 |
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| author_facet | Kunii, Daizo Levenspiel, Octave |
| author_role | aut aut |
| author_sort | Kunii, Daizo |
| author_variant | d k dk o l ol |
| building | Verbundindex |
| bvnumber | BV004593662 |
| callnumber-first | T - Technology |
| callnumber-label | TP156 |
| callnumber-raw | TP156.F65 |
| callnumber-search | TP156.F65 |
| callnumber-sort | TP 3156 F65 |
| callnumber-subject | TP - Chemical Technology |
| classification_rvk | VN 7180 |
| classification_tum | CIT 385f |
| ctrlnum | (OCoLC)263167422 (DE-599)BVBBV004593662 |
| dewey-full | 660.2842 |
| dewey-hundreds | 600 - Technology (Applied sciences) |
| dewey-ones | 660 - Chemical engineering |
| dewey-raw | 660.2842 |
| dewey-search | 660.2842 |
| dewey-sort | 3660.2842 |
| dewey-tens | 660 - Chemical engineering |
| discipline | Chemie / Pharmazie Chemie-Ingenieurwesen |
| edition | 2. ed. |
| format | Book |
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| id | DE-604.BV004593662 |
| illustrated | Illustrated |
| indexdate | 2024-07-09T16:14:45Z |
| institution | BVB |
| language | English |
| oai_aleph_id | oai:aleph.bib-bvb.de:BVB01-002824022 |
| oclc_num | 263167422 |
| open_access_boolean | |
| owner | DE-91 DE-BY-TUM DE-634 DE-83 |
| owner_facet | DE-91 DE-BY-TUM DE-634 DE-83 |
| physical | XXVII, 491 S. graph. Darst. |
| publishDate | 1991 |
| publishDateSearch | 1991 |
| publishDateSort | 1991 |
| publisher | Butterworth-Heinemann |
| record_format | marc |
| series2 | Butterworth-Heinemann series in chemical engineering |
| spelling | Kunii, Daizo Verfasser aut Fluidization engineering Daizo Kunii ; Octave Levenspiel* 2. ed. Boston u.a. Butterworth-Heinemann 1991 XXVII, 491 S. graph. Darst. txt rdacontent n rdamedia nc rdacarrier Butterworth-Heinemann series in chemical engineering Fluidization Wirbelschicht (DE-588)4066372-3 gnd rswk-swf Wirbelschichtverfahren (DE-588)4117660-1 gnd rswk-swf Wirbelschicht (DE-588)4066372-3 s DE-604 Wirbelschichtverfahren (DE-588)4117660-1 s 1\p DE-604 Levenspiel, Octave Verfasser aut HEBIS Datenaustausch Darmstadt application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=002824022&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA Inhaltsverzeichnis 1\p cgwrk 20201028 DE-101 https://d-nb.info/provenance/plan#cgwrk |
| spellingShingle | Kunii, Daizo Levenspiel, Octave Fluidization engineering Fluidization Wirbelschicht (DE-588)4066372-3 gnd Wirbelschichtverfahren (DE-588)4117660-1 gnd |
| subject_GND | (DE-588)4066372-3 (DE-588)4117660-1 |
| title | Fluidization engineering |
| title_auth | Fluidization engineering |
| title_exact_search | Fluidization engineering |
| title_full | Fluidization engineering Daizo Kunii ; Octave Levenspiel* |
| title_fullStr | Fluidization engineering Daizo Kunii ; Octave Levenspiel* |
| title_full_unstemmed | Fluidization engineering Daizo Kunii ; Octave Levenspiel* |
| title_short | Fluidization engineering |
| title_sort | fluidization engineering |
| topic | Fluidization Wirbelschicht (DE-588)4066372-3 gnd Wirbelschichtverfahren (DE-588)4117660-1 gnd |
| topic_facet | Fluidization Wirbelschicht Wirbelschichtverfahren |
| url | http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=002824022&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA |
| work_keys_str_mv | AT kuniidaizo fluidizationengineering AT levenspieloctave fluidizationengineering |