Elements of chemical reaction engineering:
Gespeichert in:
| 1. Verfasser: | |
|---|---|
| Format: | Buch |
| Sprache: | English |
| Veröffentlicht: |
Upper Saddle River, NJ
Prentice Hall
1999
|
| Ausgabe: | 3. ed. |
| Schriftenreihe: | Prentice Hall international series in the physical and chemical engineering sciences
|
| Schlagworte: | |
| Online-Zugang: | Inhaltsverzeichnis |
| Beschreibung: | XXX, 967 S. Ill., graph. Darst. 1 CD-ROM (12 cm) |
| ISBN: | 0135317088 |
Internformat
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| 245 | 1 | 0 | |a Elements of chemical reaction engineering |c H. Scott Fogler |
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| 264 | 1 | |a Upper Saddle River, NJ |b Prentice Hall |c 1999 | |
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Datensatz im Suchindex
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| adam_text | PREFACE 1 MOLE BALANCES 1.1 DEFINITION OF THE RATE OF REACTION, - R ~
2 1.2 THE GENERAL MOLE BALANCE EQUATION 6 1.3 BATCH REACTORS 8 1.4
CONTINUOUS-FLOW REACTORS 10 1.4.1 CONTINUOUS-STIRRED TANK REACTOR 10
1.4.2 TUBULAR REACTOR 11 1.4.3 PACKED-BED REACTOR 14 1.5 INDUSTRIAL
REACTORS 16 SUMMARY 25 QUESTIONS AND PROBLEMS 25 CD-ROM MATERIAL 31
SUPPLEMENTARY READING 31 2 CONVERSION AND REACTOR SIZING 2.1 DEFINITION
OF CONVERSION 33 2.2 DESIGN EQUATIONS 34 2.2.1 BUTCH SYSTEMS 34 2.2.2
FLOW SYSTEMS 37 - 2.3 APPLICATIONS OF THE DESIGN EQUATIONS FOR
CONTINUOUS-FLOW REACTORS 40 2.4 REACTORS IN SERIES 48 2.5 SOME FURTHER
DEFINITIONS 56 SUMMARY 59 VII VIII QUESTIONS AND PROBLEMS 62 CD-ROM
MATERIAL 66 SUPPLEMENTARY READING 67 3 RA TE LA WS AND STOICNIOMETR Y
BASIC DEF NITIONS 68 3.1.1 THE REACTION RATE CURLSTANT 69 3.1.2 TLZE
REACTION ORDER AND FHE RATE LAW 73 3.1.3 ELEMENTAR-Y RATE LAWS AND
MOLECULARIRY 75 3.1.4 REVERSIBLE REACTIONS 77 3.1.5 NONELENENTARY RATE
LAWS AND REACTIONS 81 PRESENT STATUS OF OUR APPROACH TO REACTOR SIZING
AND DESIGN 83 STOICHIOMETRIC TABLE 84 3.3.1 BATCH SYSTEMS 84 3.3.2
CONSTMZL-VOLUNZE REACTION SYSTEMS 87 3.3.3 FLOW SYSTEINS 90 3.3.4 WDUNE
CHANGE WITH REACTION 92 EXPRESSING CONCENTRATIONS IN TERMS OTHER THAN
CONVERSION 105 REACTIONS WITH PHASE CHANGE 107 SUMMARY 111 QUESTIONS AND
PROBLEMS 114 CD-ROM MATERIAL 123 SUPPLEMENTARY READING 123 4 ISOTHERMAL
REACTOR DESIGN DESIGN STRUCTURE FOR ISOTHERMAL REACTORS 125 SCALE-UP OF
LIQUID-PHASE BATCH REACTOR DATA TO THE DESIGN OF A CSTR 129 4.2.1 BATCH
OPERATION 129 4.2.2 DESIGN OF CSTRS 137 TUBULAR REACTORS 147 PRESSURE
DROP IN REACTORS 153 4.4.1 PRESSURE DROP AND THE RATE LAW 153 4.4.2 FLOW
THRO~~GH A PACKED BED 154 4.4.3 SPHERICAL PACKED-BED REACTORS 168 4.4.4
PRESSURE DROP IN PIPES 173 SYNTHESIZING A CHEMICAL PLANT 174 USING CA
(LIQUID) AND FA (GAS) IN THE MOLE BALANCES AND RATE LAWS 176 4.6.1
CSTRS, PFRS, PBRS, AND BATCH REACTORS 177 4.6.2 MEMBRANE REACTORS 182
UNSTEADY-STATE OPERATION OF REACTORS 187 CONTENT: CONTENTS 4.7.1
STARTUPOFACSTR 189 4.7.2 SEMIBATCH REACTORS 190 4.7.3 REACTIVE
DISTILLATION 197 4.8 RECYCLE REACTORS 200 SUMMARY 202 ODE SOLVER
ALGORITHM 204 QUESTIONS AND PROBLEMS 205 JOUR~LAL CRITIQUE PROBLEMS 219
SOME THOUGHTS ON CRITIQUING WHAT YOU READ 220 CD-ROM MATERIAL 220
SUPPLEMENTARY READING 222 COLLECTION AND ANALYSIS OF RATE DATA BATCH
REACTOR DATA 224 5.1.1 DIFFERENTIAL METHOD OF RATE ANALYSIS 224 5.1.2
HZTEGRAL METHOD 235 METHOD OF INITIAL RATES 239 METHOD OF HALF-LIVES 242
DIFFERENTIAL REACTORS 243 LEAST-SQUARE ANALYSIS 250 5.5.1 LINEARIZATION
OFTHE RATE LAW 250 5.5.2 NONLINEAR LEAST-SQUARES ANALYSIS 252 5.5.3
WEIGHTED LEAST-SQUARES ANALYSIS 261 EXPERIMENTAL PLANNING (CD-ROM) 262
EVALUATION OF LABORATORY REACTORS (CD-ROM) 263 5.7.1 INTEGRAL
(FIXED-BED) REACTOR 264 5.7.2 STIRRED BATCH REACTOR 264 5.7.3 STIRRED
CONTAINED REACTOR (SCSR) 265 5.7.4 CONTINUOUS-STIRRED TANK REACTOR
(CSTR) 265 5.7.5 STRAIGHT-THROUGH PANSPORT REACTOR 266 5.7.6
RECIRCILATINGTRARZSPNRTREACTOR 266 5.7.7 SUMMARY OF REACTOR RATINGS 267
SUMMARY 268 QUESTIONS AND PROBLEMS 269 JOURNAL CRITIQUE PROBLEMS 279
CD-ROM MATERIAL 280 SUPPLEMENTAIY READING 280 MULTIPLE REACTIONS 6.1
PARALLEL REACTIONS 284 6.1.1 MAXIMIZING THE DESIRED PRODUCT FOR ONE
REACTANT 285 6.1.2 MAXIMIZING THE RATE SELECTIVITY PARAMETER S FOR TWO
REACTANTS 288 CONTENTS MAXIMIZING THE DESIRED PRODUCT IN SERIES
REACTIONS 291 ALGORITHM FOR SOLUTION TO COMPLEX REACTIONS 295 6.3.1 MOLE
BALRZNCES 295 6.3.2 NET RATES QF REACTION 296 6.3.3 RATE LAWS 297 6.3.4
STOICHIOMETRY: RELATIVE RATES OF REACTION 6.3.5 STOICHIOINETLY:
CONCENTRATIONS 300 6.3.6 COMBIRZITZG STEP 3301 6.3.7 MULTILDE REACTIONS
IN A CSTR 307 SORTING IT ALL OUT 314 THE FUN PART 315 THE ATTAINABLE
REGION CD-ROM 316 S~~MRNARY 318 QUESTIONS AND PROBLEMS 320 JOURNAL
CRITIQUE PROBLEMS 335 CD-ROM MATERIAL 335 SUPPLEMENTARY READING 336 7
NUNELEMENTARY REACTION KINETICS FUNDAMENTALS 340 7.1. I ACTIVE
INTERMEDICRTES 340 7.1.2 PSEUDO-STEADY-STATE HYPOTHESIS (PSSH) SEARCHING
FOR A MECHANISM 344 7.2.1 GENERAL CONSICLERCITIONS 344 7.2.2 REACTION
PATHWAYS 352 POLYMERIZATION 354 7.3.1 STEP POLYMERIZUTION 356 7.3.2
CHAIN POLYMERIZ~LTIONS REACTIONS 360 7.3.3 MODELING A BATCH
POLYMERIZATION REACTOR 7.3.4 MOLECIILAR WEIGHT DISTRIBUTION 370 7.3.5
ANIONIC POLYMERIZATION 375 ENZYMATIC REACTION FUNDAMENTALS 383 7.4.1
DEFINITIONS AND MECHANISNZS 383 7.4.2 MICHAELIS-MENTERZ EQCINTION 386
7.4.3 BATCH REACTOR CALCILATIONS 389 7.4.4 INHIBITION OF ENZYME
REACTIONS 391 7.4.5 MULTIPLE ENZYME AND SUBSTRATE SYSTEMS BIOREACTORS
393 7.5.1 CELL GROWTH 394 7.5.2 RARE LAWS 396 7.5.3 STOICHIOMETRY 398
7.5.4 MASS BALANCES 400 7.5.5 CLZEN~OSTATS 404 7.5.6 DESIGN EQUATIONS
404 7.5.7 WASH-OUT 406 CONTENTS 7.5.8 OXYGEN-LIMITED FERMENTATION 407
7.5.9 SCALE-UP 407 SUMMARY 408 QUESTIONS AND PROBLEMS 410 CD-ROM
MATERIAL 423 JOURNAL CRITIQUE PROBLEMS 424 SUPPLEMENTARY READING 424
STEADY-STATE NONISOTHERMAL REACTOR DESIGN RATIONALE 426 THE ENERGY
BALANCE 427 8.2.1 FIRST LAW THERMODYNAMICS 427 8.2.2 EVALUATING THE WORK
TERM 429 8.2.3 DISSECTING THE STEADY-STATE MOLAR FLOW RATES TO OBTAIN
THE HEAT OF REACTION 430 8.2.4 DISSECTING THE ENTHALPIES 432 8.2.5
RELATING GHK(T), 6HOK, AND 6CP 434 8.2.6 CONSTANT OF MEAN HEAT
CAPACITIES 435 8.2.7 VARIABLE HEAT CAPACITIES 436 8.2.8 HEAT ADDED TO
THE REACTOL; Q 438 NONISOTHERMAL CONTINUOUS-FLOW REACTORS 440 8.3.1
APPLICATION TO THE CSTR 441 8.3.2 ADIABATIC TUBULAR REACTOR 451 8.3.3
STEADY-STATE TUBULAR REACTOR WITH HEAT EXCHANGE 458 EQUILIBRIUM
CONVERSION 468 8.4.1 ADIABATIC TEMPERATURE AND EQUILIBRIUM CONVERSION
468 8.4.2 OPTIMUM FEED TEMPERATURE 476 NONADIABATIC REACTOR OPERATION:
OXIDATION OF SULFUR DIOXIDE EXAMPLE 478 8.5.1 MANUFACTURE OF SULFURIC
ACID 478 8.5.2 CATALYST QUANTITIES 481 8.5.3 REACTOR CONFIGURATION 482
8.5.4 OPERATING CONDITIONS 482 MULTIPLE STEADY STATES 490 8.6.1
HEAT-REMOVED TERM, R(T) 491 8.6.2 HEAT OF GENERATION, G(T) 492 8.6.3
IGNITION-EXTINCTION CURVE 493 8.6.4 RUNAWAY REACTIONS 497 8.6.5
STEADY-STATE BIFIRCATION ANALYSIS 498 NONISOTHERMAL MULTIPLE CHEMICAL
REACTIONS 500 8.7.1 PLUG-FLOW REACTORS 500 8.7.2 CSTR 504 SUMMARY 507
XII CONTENTS QUESTIONS AND PROBLEMS 511 JOURNAL CRITIQUE PROBLEMS 530
CD-ROM MATERIAL 530 SUPPLEMENTARY READING 532 9 UNSTEADY-STATE
NONISOTHERMAL REACTOR DESIGN THE GENERAL EQUATION 534 UNSTEADY OPERATION
OF CSTRS AND SEMIBATCH REACTORS 535 9.2.1 BATCH REACTORS 537 9.2.2
ADIABATIC OPERATION OF A BATCH REACTOR 537 9.2.3 TRANSIENT CSTR, BALCH,
AND SEMIBATCH REACTORS WITH HEAT EXCHANGER-AMBIENT TEMPERATURE NOT
SPATIALLY UNIFORM 548 APPROACH TO THE STEADY STATE 553 CONTROL OF
CHEMICAL REACTORS 558 9.4.1 FALLING OFTHE STEADY STATE 558 9.4.2 ADDING
A CONTROLLER TO A CSTR 561 NONISOTHERN~AL MULTIPLE REACTIONS 566
UNSTEADY OPERATION OF PLUG-FLOW REACTORS 570 SUMMARY 571 QUESTIONS AND
PROBLEMS 572 CD-ROM MATERIAL 579 SUPPLEMENTARY READING 579 10 CATALYSIS
AND CATALYTIC REACTORS 10.1 CATALYSTS 581 10.1.1 DEJNITIONS 582 10.1.2
CATALYST PROPERTIES 583 10.2 STEPS IN A CATALYTIC REACTION 591 10.2.1
ADSORPTION ISOTHERMS 594 10.2.2 SURJ%CE REACTION 599 10.2.3 DESORPTION
601 10.2.4 THE RATE-LIMITING STEP 601 10.3 SYNTHESIZING A RATE LAW,
MECHANISM, AND RATE-LIMITING STEP 603 10.3.1 IS THE ADSORPTION OF
CUNZENE RATE-LIMITING? 606 10.3.2 IS THE SURFACE REACTION RATE-LIMITING
Y 609 10.3.3 IS THE DESORPTION OF BENZENE RATE-LIMITING? 610 10.3.4
SURNINARY OF THE CUMENE DECOMPOSITION 612 10.3.5 RARE LAWS DERIVED FROM
THE PSEUDO-STEADY-STATE HYPOTHESIS 616 10.4 DESIGN OF REACTORS FOR
GAS-SOLID REACTIONS 619 10.4.1 BASIC GUIDELINES 619 10.4.2 THE DESIGN
EQUATIONS 619 XIII 10.5 HETEROGENEOUS DATA ANALYSIS FOR REACTOR DESIGN
10.5.1 DEDUCING A RATE LAW FROM THE EXPERIMENTAL DATA 622 10.5.2 FINDING
A MECHANISM CONSISTENT WITH EXPERIMENTAL OBSERVATIONS 623 10.5.3
EVALUATION OF THE RATE LAW PARAMETERS 10.5.4 REACTOR DESIGN 627 10.6
CHEMICAL VAPOR DEPOSITION 631 10.7 CATALYST DEACTIVATION 634 10.7.1
TYPES OF CATALYST DEACTIVATION 636 10.7.2 TEMPERATURE-TIME TRAJECTORIES
647 10.7.3 MOVING-BED REACTORS 649 10.7.4 SMIGHT- TLZROUGLZ TRANSPORT
REACTORS 655 10.7.5 DETERMINING THE ORDER OJDCACTIVATION 660 10.8
REACTION ENGINEERING IN MICROELECTRONIC DEVICE FABRICATION 662 10.8.1
ETCHING 664 SUMMARY 665 QUESTIONS AND PROBLENLS 668 JOURNAL CRITIQUE
PROBLEMS 682 CD-ROM MATERIAL 683 SUPPLEMENTARY READING 684 EXTERNAL
DIFFUSION EFFECTS ON HETEROGENEOUS REACTIONS 1 1.1 MASS TRANSFER
FUNDAMENTALS 687 11.1.1 DEFINITIONS 687 11.1.2 MOLAR FLUX 687 11.1.3
FICKS FIRST LAW 688 1 1.2 BINARY DIFFUSION 689 11.2.1 EVALUATING THE
MOLAR FLUX 689 11.2.2 BOUNDARY CONDITIONS 692 11.2.3 MODELING DIFFUSION
WITHOUT REACTION 692 11.2.4 TEMPERATURE AND PRESSURE DEPENDENCE OF DAB
697 11.2.5 MODELING DIFF~~SION WITH CLZENZICCZL REACTION 698 1 1.3
EXTERNAL RESISTANCE TO MASS TRANSFER 699 11.3.1 MASS TRANSFER COEFHCIENT
699 11.3.2 MASS TRANSFER TO A SINGLE PARTICLE 702 11.3.3 MASS
TRANSFER-LIRNITED REACTIONS IN PACKED BEDS 706 11.3.4 MASS
TRANSFER-LIMITED REACTION ON METALLIC SURJGACES 714 11.4 WHAT IF ... ?
(PARAMETER SENSITIVITY) 715 11.5 THE SHRINKING CORE MODEL 719 XIV
CONTENTS CATALYST REGENERATION 720 DISSOLUTION OF MONODISPERSED SOLID
PARTICLES 724 FLOW AND DISSOLUTION IN POROUS MEDIA 726 SUMMARY 728
QUESTIONS AND PROBLEMS 729 JOURNAL ARTICLE PROBLEM 735 JOURNAL CRITIQUE
PROBLEMS 735 CD-ROM MATERIAL 735 SUPPLEMENTARY READING 736 12 DIFFUSION
AND REACTION IN POROUS CATALYSTS DIFFUSION AND REACTION IN SPHERICAL
CATALYST PELLETS 739 12.1.1 EFFECTIVE DIJ%SIVITY 739 12.1.2 DERIVATION
OF THE DIFSERENTIAL EQUATION DESCRIBING DIFISION AND REACTION 741 12.1.3
WRITING THE EQUATION IN DIMENSIONLESS FORM 743 12.1.4 SOLUTION TO THE
DIFSERENTIAL EQUATION FOR A FIRST-ORDER REACTION 746 INTERNAL
EFFECTIVENESS FACTOR 747 FALSIFIED KINETICS 753 OVERALL EFFECTIVENESS
FACTOR 755 ESTIMATION OF DIFFUSION- AND REACTION-LIMITED REGIMES 758
12.5.1 WEISZ-PRATER CRITERION FOR INTERNAL DIFFBSION 758 12.5.2 MEARS
CRITERION FOR EXTERNAL DIFFUSION 761 MASS TRANSFER AND REACTION IN A
PACKED BED 761 DETERMINATION OF LIMITING SITUATIONS FROM REACTION DATA
767 MULTIPHASE REACTORS 768 12.8,1 SLURRY REACTORS 769 12.8.2 TRICKLE
BED REACTORS 783 FLUIDIZED-BED REACTOR^^^-^^^ 786 THE OVERALL VIEW 787
CHEMICAL VAPOR DEPOSITION REACTORS 789 SUMMARY 793 QUESTIONS AND
PROBLEMS 795 JOURNAL ARTICLE PROBLEMS 804 JOURNAL CRITIQUE PROBLEMS 805
CD-ROM MATERIAL 805 SUPPLEMENTARY READING 806 13 DISTRIB UTZONS OF
RESIDENCE TIMES FOR CHEMICAL REACTORS 13.1 GENERAL CHARACTERISTICS 809
13.1.1 RESIDENCE-TIME DISTRIBUTION FUNCTION 811 CONTENTS 13.2
MEASUREMENT OF THE RTD 812 23.2.1 PULSE INPUT 813 13.2.2 STEP TRACER
EXPERIMENT 8 18 13.3 CHARACTERISTICS OF THE RTD 819 13.3.1 INTEGRAL
RELATIONSHIPS 819 13.3.2 MEAN RESIDENCE TIME 821 13.3.3 OTHER MOMENTS OF
THE RTD 823 13.3.4 NORMALIZED RTD FUNCTION, E(0) 825 13.3.5 INTERNAL-AGE
DISTRIBUTION I(A) 826 13.4 RTD IN IDEAL REACTORS 829 13.4.1 RTDS IN
BATCH AND PLUG-FLOW REACTORS 829 13.4.2 SINGLE-CSTR RTD 829 13.4.3
LAMINAR FLOW REACTOR 831 13.4.4 PFRLCSTR SERIES RTD 833 13.5 REACTOR
MODELING WITH THE RTD 836 13.6 ZERO-PARAMETER MODELS 838 13.6.1
SEGREGATION MODEL 838 13.6.2 MAXIMUM MIXEDNESS 844 13.63 HEAT EFFECTS
851 13.7 USING SOFTWARE PACKAGES 851 13.8 RTD AND MULTIPLE REACTIONS 854
13.8.1 SEGREGATION MODEL 854 13.8.2 MAXIMUM MIXEDNESS 855 SUMMARY 860
QUESTIONS AND PROBLEMS 861 CD-ROM MATERIAL 868 SUPPLEMENTARY READING 869
14 MODELS FOR NONZDEAL REACTORS 14.1 SOME GUIDELINES 871 14.2
ONE-PARAMETER MODELS 872 14.2.1 TANKS-IN-SERIES MODEL 873 14.2.2
DISPERSION MODEL 877 14.3 TWO-PARAMETER MODELS-MODELING REAL REACTORS
WITH COMBI- NATIONS OF IDEAL REACTORS 893 14.3.1 REAL CSTR MODELED USING
BYPASSING AND DEAD SPACE 893 14.3.1A SOLVING THE MODEL SYSTEM FOR CA AND
X 894 14.3.1B USING A TRACER TO DETERMINE THE MODEL PARAMETERS IN CSTR-W
ITH-DEAD-SPACE-AND-BYPASS MODEL 895 14.3.2 REAL CSTR MODELED WITH AN
EXCHANGE VOLUME 899 L4.3.2A SOLVING THE MODEL SYSTEM FOR CA AND X 900
CONTENTS APPENDIX A APPENDIX B APPENDIX C APPENDIX D APPENDIX E APPENDIX
F APPENDIX G APPENDIX H 14.3.2B U.SII,Q (1 POCPI TO DPTERRLLIL?~ TJ7E
MODEL PARMIRTRRS IN ~1 CSTR WITH M7 EXC-LZANGE VOLUME 900 14.4 USE OF
SOFTWARE PACKAGES TO DETERMINE THE MODEL PARAMETERS 901 14.5 OTHER
MODELS OF NONIDEAL REACTORS USING CSTRS AND PFRS 904 14.6 USING THE RTD
VERSUS NEEDING A MODEL 904 SUMMARY 907 QUESTIOI~S AND PROBLEMS 909
CD-ROM MATERIAL 916 SUPPLEMENTARY READING 917 NUMERICAL TECHNIQUES A. 1
USEFUL INTEGRALS IN REACTOR DESIGN 921 A.2 EQUAL-AREA GRAPHICAL
DIFFERENTIATION 922 A.3 SOLUTIONS TO DIFFERENTIAL EQUATIONS 924 A.4
NU~RERICAL EVALUATION OF INTEGRALS 924 AS SOFTWARE PACKAGES 926 IDEAL
GAS CONSTANT AND CONVERSION FACTORS THERMODYNAMIC RELATIONSHIPS
INVOLVING THE EQUILIBRIUM CONSTANT 929 MEASUREMENT OF SLOPES ON SEMILOG
PAPER 935 SOFTWARE PACKAGES 936 NOMENCLATURE 938 MOLECULAR DYNAMICS OF
CHEMICAL REACTIONS 941 G. 1 COLLISION THEORY 941 G.2 TRANSITION STATE
THEORY 944 G.3 MOLECULAR DYNAMICS 948 OPEN-ENDED PROBLEMS H. 1 DESIGN OF
REACTION ENGINEERING EXPERIMENT 953 H.2 EFFECTIVE LUBRICANT DESIGN 953
H.3 PEACH BOTTOM NUCLEAR REACTOR 953 CONTENTS XVII H.4 UNDERGROUND WET
OXIDATION 954 H.5 HYDROSULFURIZATION REACTOR DESIGN 954 H.6 CONTINUOUS
BIOPROCESSING 954 H.7 METHANOL SYNTHESIS 954 H.8 CAJUN SEAFOOD GUMBO 954
APPENDIX I HOW TO USE THE CD-ROM CD 1 COMPONENTS OF THE CD-ROM CD2
INTERACTIVE LECTURE NOTES AUDIOS . , EQUATION DERIVATION , CD3
FREQUENTLY ASKED QUESTIONS CD4 LIVING EXAMPLE PROBLEMS CD5 PROFESSIONAL
REFERENCE SHELF CD6 ADDITIONAL HOME PROBLEMS CD7 NAVIGATION CD8
INTERACTIVE COMPUTER PROBLEMS (ICM S) [E.G., ICM SIMULATION, HEAT
EFFECTS SHOWN BELOW] ICM-HEAT EFFECTS 1 APPENDIX J USE OF COMPUTATIONAL
CHEMLSTRY SOFTWARE PACKAGES 958 INDEX 961 ABOUT THE CD 976
|
| any_adam_object | 1 |
| author | Fogler, H. Scott |
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| author_role | aut |
| author_sort | Fogler, H. Scott |
| author_variant | h s f hs hsf |
| building | Verbundindex |
| bvnumber | BV012650122 |
| callnumber-first | T - Technology |
| callnumber-label | TP157 |
| callnumber-raw | TP157 |
| callnumber-search | TP157 |
| callnumber-sort | TP 3157 |
| callnumber-subject | TP - Chemical Technology |
| classification_rvk | VN 7300 VN 7301 |
| ctrlnum | (OCoLC)247730560 (DE-599)BVBBV012650122 |
| dewey-full | 660.28 |
| dewey-hundreds | 600 - Technology (Applied sciences) |
| dewey-ones | 660 - Chemical engineering |
| dewey-raw | 660.28 |
| dewey-search | 660.28 |
| dewey-sort | 3660.28 |
| dewey-tens | 660 - Chemical engineering |
| discipline | Chemie / Pharmazie |
| edition | 3. ed. |
| format | Book |
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| id | DE-604.BV012650122 |
| illustrated | Illustrated |
| indexdate | 2024-07-09T18:31:16Z |
| institution | BVB |
| isbn | 0135317088 |
| language | English |
| oai_aleph_id | oai:aleph.bib-bvb.de:BVB01-008594419 |
| oclc_num | 247730560 |
| open_access_boolean | |
| owner | DE-703 DE-83 |
| owner_facet | DE-703 DE-83 |
| physical | XXX, 967 S. Ill., graph. Darst. 1 CD-ROM (12 cm) |
| publishDate | 1999 |
| publishDateSearch | 1999 |
| publishDateSort | 1999 |
| publisher | Prentice Hall |
| record_format | marc |
| series2 | Prentice Hall international series in the physical and chemical engineering sciences |
| spelling | Fogler, H. Scott Verfasser aut Elements of chemical reaction engineering H. Scott Fogler 3. ed. Upper Saddle River, NJ Prentice Hall 1999 XXX, 967 S. Ill., graph. Darst. 1 CD-ROM (12 cm) txt rdacontent n rdamedia nc rdacarrier Prentice Hall international series in the physical and chemical engineering sciences Reaktionstechnik (DE-588)4136173-8 gnd rswk-swf Chemische Verfahrenstechnik (DE-588)4069941-9 gnd rswk-swf Chemischer Reaktor (DE-588)4121085-2 gnd rswk-swf Reaktionstechnik (DE-588)4136173-8 s Chemischer Reaktor (DE-588)4121085-2 s Chemische Verfahrenstechnik (DE-588)4069941-9 s 1\p DE-604 OEBV Datenaustausch application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=008594419&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 | Fogler, H. Scott Elements of chemical reaction engineering Reaktionstechnik (DE-588)4136173-8 gnd Chemische Verfahrenstechnik (DE-588)4069941-9 gnd Chemischer Reaktor (DE-588)4121085-2 gnd |
| subject_GND | (DE-588)4136173-8 (DE-588)4069941-9 (DE-588)4121085-2 |
| title | Elements of chemical reaction engineering |
| title_auth | Elements of chemical reaction engineering |
| title_exact_search | Elements of chemical reaction engineering |
| title_full | Elements of chemical reaction engineering H. Scott Fogler |
| title_fullStr | Elements of chemical reaction engineering H. Scott Fogler |
| title_full_unstemmed | Elements of chemical reaction engineering H. Scott Fogler |
| title_short | Elements of chemical reaction engineering |
| title_sort | elements of chemical reaction engineering |
| topic | Reaktionstechnik (DE-588)4136173-8 gnd Chemische Verfahrenstechnik (DE-588)4069941-9 gnd Chemischer Reaktor (DE-588)4121085-2 gnd |
| topic_facet | Reaktionstechnik Chemische Verfahrenstechnik Chemischer Reaktor |
| url | http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=008594419&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA |
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