Multicomponent mass transfer:
Gespeichert in:
Hauptverfasser: | , |
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Format: | Buch |
Sprache: | English |
Veröffentlicht: |
New York [u.a.]
Wiley
1993
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Schriftenreihe: | Wiley series in chemical engineering
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Schlagworte: | |
Online-Zugang: | Inhaltsverzeichnis |
Beschreibung: | Hier auch später erschienene, unveränderte Nachdrucke |
Beschreibung: | XXXIV, 579 S. graph. Darst. 1 Diskette, 3,5" |
ISBN: | 0471574171 9780471574170 |
Internformat
MARC
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245 | 1 | 0 | |a Multicomponent mass transfer |c Ross Taylor ; R. Krishna |
264 | 1 | |a New York [u.a.] |b Wiley |c 1993 | |
300 | |a XXXIV, 579 S. |b graph. Darst. |e 1 Diskette, 3,5" | ||
336 | |b txt |2 rdacontent | ||
337 | |b n |2 rdamedia | ||
338 | |b nc |2 rdacarrier | ||
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700 | 1 | |a Krishna, Rajamani |e Verfasser |4 aut | |
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Datensatz im Suchindex
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adam_text | CONTENTS
Nomenclature xxv
PARTI MOLECULAR DIFFUSION 1
1 Preliminary Concepts
1 1 Concentration Measures, 3
1 2 Fluxes, 3
121 Transformations Between Fluxes, 6
1 3 Balance Relations for a Two-Phase System Including a Surface
of Discontinuity, 9
1 4 Summary, 12
2 The Maxwell-Stefan Relations
2 1 Diffusion in Ideal Gas Mixtures, 13
211 The Mechanics of Molecular Collisions, 13
212 Derivation of the Maxwell-Stefan Equation for Binary
Diffusion, 14
213 The Maxwell-Stefan Equations for Ternary Systems, 17
214 The Maxwell-Stefan Equations for Multicomponent
Systems, 19
215 Matrix Formulation of the Maxwell-Stefan
Equations, 19
IK -
Example 211 Multicomponent Diffusion
in a Stefan Tube: An Experimental Test
of the Maxwell-Stefan Equations, 21
Diffusion in Nonideal Fluids, 23
221 Matrix Formulation of the Maxwell-Stefan Equations
for Nonideal Fluids, 25
222 Limiting Cases of the Maxwell-Stefan Equations, 25
Example 221 Diffusion of Toluene
in a Binary Mixture, 26
The Generalized Maxwell-Stefan Formulation of Irreversible
Thermodynamics, 28
231 The Generalized Driving Force, 28
232 The Generalized Maxwell-Stefan Equations, 30
xiii
xiv CONTENTS
233 An Application of the Generalized Maxwell-Stefan
Equations—The Ultracentrifuge, 32
Example 231 Ultracentrifugation of a Binary liquid
Mixture, 34
Example 232 Separation of Uranium Isotopes
With a Gaseous Ultracentrifuge, 36
2 4 Diffusion in Electrolyte Systems, 37
241 The Nemst-Planck Equation, 40
Example 241 Diffusion in the System KC1 — H20
at 25°C, 41
242 Conductivity, Transference Numbers, and the Diffusion
Potential, 43
243 Effective Ionic Diffusivities, 45
Example 242 Diffusion in an Aqueous Solution of HC1
and BaCl2, 46
3 Fick’s Law 50
3 1 Diffusion in Binary Mixtures: Fick’s First Law, 50
311 Fick Diffusion Coefficients, 50
312 Alternative Forms of Fick’s Law, 51
3 2 The Generalized Fick’s Law, 52
321 Matrix Representation of the Generalized Fick’s Law, 53
322 Alternative Forms of the Generalized Fick’s Law, 54
323 Multicomponent Fick Diffusion Coefficients, 54
324 Transformation of Multicomponent Diffusion Coefficients
From One Reference Velocity Frame to Another, 56
Example 321 Fick Diffusion Coefficients for the System
Acetone-Benzene-Methanol, 57
3 3 Irreversible Thermodynamics and the Generalized Fick’s Law, 59
Example 331 Calculation of the Onsager Coefficients, 61
331 Diffusion in the Region of a Critical Point, 62
4 Estimation of Diffusion Coefficients 67
4 1 Diffusion Coefficients in Binary Mixtures, 67
411 Relationship Between Fick and Maxwell-Stefan Diffusion
Coefficients, 67
412 Estimation of Diffusion Coefficients in Gas Mixtures, 68
413 Diffusion Coefficients in Binary Liquid Mixtures, 69
414 Estimation of Diffusion Coefficients in Dilute Liquid
Mixtures, 73
Example 411 Diffusion of Alcohols Infinitely Diluted
in Water, 75
415 Estimation of Diffusion Coefficients in Concentrated
Liquid Mixtures, 76
^
^
-
-
A
„
t
CONTENTS xv
Example 412 Diffusion Coefficients in the System
Acetone-Benzene, 77
Example 413 Diffusion Coefficients in the System
Ethanol-Water, 78
Estimation of Multicomponent Diffusion Coefficients, 79
Estimation of Multicomponent Diffusion Coefficients
for Gas Mixtures, 80
Example 421 The Structure of the Fick Matrix [D]
When All of the Binary Diffusion Coefficients
are Nearly Equal, 81
Example 422 [D] for Dilute Gas Mixtures, 82
Example 423 Composition Dependence of the Fick
Matrix [D], 82
Example 424 Effect of Component Numbering
on the Fick Matrix, 84
Example 425 Prediction of Multicomponent Diffusion
Coefficients in the Mass Average Reference Velocity
Frame, 86
Estimation of Multicomponent Fick Diffusion Coefficients
for Liquid Mixtures, 88
Estimation of Maxwell-Stefan Diffusion Coefficients
for Multicomponent Liquid Mixtures, 89
Example 426 Prediction of [D] in the System
Acetone-Benzene-Carbon Tetrachloride, 91
Maxwell-Stefan, Fick, and Onsager Irreversible
Thermodynamics Formulations: A Summary Comparison, 93
5 Solution of Multicomponent Diffusion Problems: The Linearized Theory 95
5 1 Mathematical Preliminaries, 95
511 The Binary Diffusion Equations, 95
512 The Multicomponent Diffusion Equations, 96
513 Solving the Multicomponent Equations, 97
514 Special Relations for Ternary Systems, 99
5 2 Interaction Effects, 100
5 3 Steady State Diffusion, 102
Example 531 Steady-State Diffusion in a Ternary
System, 103
5 4 Diffusion in a Two Bulb Diffusion Cell, 105
541 Binary Diffusion in a Two Bulb Diffusion Cell, 106
542 Multicomponent Diffusion in a Two Bulb
Diffusion Cell, 106
Example 541 Multicomponent Diffusion in a Two Bulb
Diffusion Cell: An Experimental Test of the Linearized
Theory, 107
xvi CONTENTS
5 5 The Loschmidt Tube, 110
Example 551 Multicomponent Diffusion in the Loschmidt
Tube: Another Test for the Linearized Theory, 112
5 6 Multicomponent Diffusion in a Batch Extraction Cell, 115
561 Equilibration Paths, 115
Example 561 Equilibration Paths in a Batch Extraction
Cell, 118
562 Equilibration Paths in the Vicinity of the Plait Point, 121
5 7 The Linearized Theory: An Appraisal, 122
6 Solution of Multicomponent Diffusion Problems: Effective Diffiisivity
Methods 124
6 1 The Effective Diffusivity, 124
611 Definitions, 124
612 Relationship Between Effective, Maxwell-Stefan, and
Multicomponent Fick Diffusion Coefficients, 125
613 Limiting Cases, 126
Example 611 Computation of the Effective
Diffusivity, 127
6 2 Solution of Multicomponent Diffusion Problems Using
an Effective Diffusivity Model, 129
6 3 Steady-State Diffusion, 129
Example 631 Computation of the Fluxes with
an Effective Diffusivity Model, 130
6 4 The Two Bulb Diffusion Cell, 131
Example 641 Diffusion in a Two Bulb Diffusion Cell:
A Test of the Effective Diffusivity, 131
6 5 The Loschmidt Tube, 133
Example 651 Multicomponent Diffusion in the Loschmidt
Tube: Another Test of the Effective Diffusivity, 134
6 6 Diffusion in a Batch Extraction Cell, 136
Example 661 Multicomponent Diffusion in a Batch
Extraction Cell, 136
6 7 The Effective Diffusivity—Closing Remarks, 138
PART II INTERPHASE TRANSFER 139
7 Mass Transfer Coefficients 141
7 1 Definition of Mass Transfer Coefficients, 141
711 Binary Mass Transfer Coefficients, 141
712 Multicomponent Mass Transfer Coefficients, 143
713 Interaction Effects (Again), 144
CONTENTS xvii
7 2 The Bootstrap Problem (and Its Solution), 145
721 Equimolar Counterdiffusion, 145
722 Multicomponent Distillation, 145
723 Stefan Diffusion, 146
724 Flux Ratios Specified, 146
725 The Generalized Bootstrap Problem, 147
726 The Bootstrap Matrix, 148
7 3 Interphase Mass Transfer, 149
731 Overall Mass Transfer Coefficients, 150
Film Theory 152
8 1 The Film Model, 152
8 2 Film Model for Binary Mass Transfer, 153
821 Equimolar Counterdiffusion, 156
822 Stefan Diffusion, 156
823 Flux Ratios Fixed, 156
824 Generalization to Other Geometries, 156
Example 821 Equimolar Distillation of a Binary
Mixture, 157
Example 822 Production of Nickel Carbonyl, 158
Example 823 Condensation of a Binary Vapor
Mixture, 160
8 3 Exact Solutions of the Maxwell-Stefan Equations
for Multicomponent Mass Transfer in Ideal Gases, 162
831 Formulation in Terms of Binary Mass Transfer
Coefficients, 165
832 Limiting Cases of the General Solution, 167
833 Computation of the Fluxes, 168
Example 831 Equimolar Counterdiffusion in a Ternary
Mixture, 170
Example 832 Diffusional Distillation, 174
834 Advanced Computational Strategies, 179
835 An Alternative Formulation, 182
8 4 Multicomponent Film Model Based on the Assumption
of Constant [D] Matrix: The Linearized Theory of Toor,
Stewart, and Prober, 184
841 Comparison with Exact Method, 185
842 The Toor-Stewart-Prober Formulation, 187
843 Computation of the Fluxes, 189
Example 841 Vapor-Phase Dehydrogenation
of Ethanol, 191
8 5 Simplified Explicit Methods, 196
851 Method of Krishna, 197
852 Method of Burghardt and Krupiczka, 197
853 Method of Taylor and Smith, 199
xviii CONTENTS
854 Computation of the Fluxes, 200
Example 851 Evaporation into Two Inert Gases, 201
855 Comparison With Exact and Linearized Solutions, 203
8 6 Effective Diffusivity Methods, 204
Example 861 Diffusion in a Stefan Tube, 206
861 Comparison With the Matrix Methods, 208
8 7 Multicomponent Film Models for Mass Transfer in Nonideal
Fluid Systems, 209
871 Exact Solutions, 209
872 Approximate Methods, 209
Example 871 Mass Transfer in a Nonideal Fluid
Mixture, 211
8 8 Estimation of Mass Transfer Coefficients from Empirical
Correlations, 212
881 Estimation of Binary Mass Transfer Coefficients, 213
882 Estimation of Multicomponent Mass Transfer Coefficients:
The Method of Toor, Stewart, and Prober, 214
883 Estimation of Multicomponent Mass Transfer
Coefficients for Gas Mixtures from Binary Mass
Transfer Coefficients, 215
884 Estimation of Mass Transfer Coefficients for Nonideal
Multicomponent Mixtures, 216
Example 881 Ternary Distillation in a Wetted Wall
Column, 216
885 Estimation of Overall Mass Transfer Coefficients:
A Simplified Result, 219
9 Unsteady-State Mass Transfer Models
9 1 Surface Renewal Models, 220
9 2 Unsteady-State Diffusion in Binary Systems, 222
Example 9,2 1 Regeneration of Triethylene Glycol, 225
9 3 Unsteady-State Diffusion in Multicomponent Systems, 228
931 An Exact Solution of the Multicomponent Penetration
Model, 228
932 Multicomponent Penetration Model Based
on the Assumption of Constant [D] Matrix, 230
933 Toor-Stewart-Prober Formulation, 232
Example 931 Mass Transfer in a Stirred Cell, 233
9 4 Diffusion in Bubbles, Drops, and Jets, 235
941 Binary Mass Transfer in Spherical and Cylindrical
Geometries, 235
942 Transport in Multicomponent Drops and Bubbles, 238
Example 941 Diffusion in a Multicomponent Drop, 239
CONTENTS xix
10 Mass Transfer in Turbulent Flow
10 1 Balance and Constitutive Relations for Turbulent Mass
Transport, 242
10 2 Turbulent Eddy Diffusivity Models, 244
10 2 1 Estimation of the Turbulent Eddy Viscosity, 246
10 3 Turbulent Mass Transfer in a Binary Fluid, 248
10 3 1 Solution of the Diffusion Equations, 248
10 3 2 Mass Transfer Coefficients, 250
Example 10 3 1 Thin Film Sulfonation of DodeCyl
Benzene, 252
10 4 Turbulent Eddy Transport in Multicomponent Mixtures, 255
10 4 1 Solution of the Multicomponent Diffusion
Equations, 255
10 4 2 Multicomponent Mass Transfer Coefficients, 257
10 4 3 Computational Issues, 258
Example 10 4 1 Methanation in a Tube
Wall Reactor, 259
10 4 4 Comparison of the Chilton-Colburn Analogy
with Turbulent Eddy Diffusivity Based Models, 264
11 Simultaneous Mass and Energy Transfer
11 1 Balance Equations for Simultaneous Heat and
Mass Transfer, 266
11 2 Constitutive Relations for Simultaneous Heat and
Mass Transfer, 267
11 3 Definition of Heat Transfer Coefficients, 269
11 4 Models for Simultaneous Heat and Mass Transfer, 270
11 4 1 The Film Model, 270
Example 11 4 1 Heat Transfer in Diffusional
Distillation, 273
11 4 2 The Penetration Model, 274
11 4 3 Turbulent Eddy Diffusivity Model, 274
Example 11 4 2 Estimation of the Heat Transfer
Coefficient in a Thin-Film Sulfonator, 277
11 4 4 Empirical Methods, 278
11 5 Interphase Mass and Energy Transfer, 279
11 5 1 The Bootstrap Problem Revisited, 281
11 5 2 Nonequimolar Effects in Multicomponent Distillation, 282
Example 11 5 1 Nonequimolar Effects in Ternary
Distillation, 283
11 5 3 Computation of the Fluxes, 285
Example 11 5 2 Distillation of a Binary Mixture, 287
Example 11 5 3 Interphase Mass Transfer in the Presence
of an Inert Gas, 292
XX CONTENTS
PART Ul DESIGN 305
12 Multicomponent Distillation: Mass Transfer Models 307
12 1 Binary Distillation in Tray Columns, 307
12 1 1 Material Balance Relations, 309
12 1 2 Composition Profiles, 310
12 1 3 Mass Transfer Rates, 310
12 1 4 Numbers of Transfer Units, 311
12 1 5 Numbers of Transfer Units from Empirical
Correlations, 312
Example 12 1 1 Distillation of
Toluene-Methylcyclohexane, 314 ; ,
12 1 6 Numbers of Transfer Units—A Simplified Approach, 317
12 17A Fundamental Model of Tray Performance, 318 M
Example 12 1 2 Regeneration of Triethylene Glycol, *324
12 2 Multicomponent Distillation in Tray Columns, 330
12 2 1 Composition Profiles, 330
12 2 2 Mass Transfer Rates, 332 *
12 2 3 Numbers of Transfer Units for Multicomponent
Systems, 333
Example 12 2 1 Numbers of Transfer Units }■
Methanol-l-Propanol-Water Systems, 33| - mrL-H
12 24A Fundamental Model of Mass Transfer *
in Multicomponent Distillation, 336 1 ^
Example 12 2 2 Distillation of Ethanol-terf-
Alcohol-Water in a Sieve Tray Column, 339
12 3 Distillation in Packed Columns, 348
12 3 1 Material and Energy Balance Relations, 350
12 3 2 Transfer Units for Binary Systems, 353 ^
12 3 3 Mass Transfer Coefficients for Packed Columns, T 355
Example 12 3 1 Distillation of Acetone-Water •
in a Packed Column, 358 ^
Example 12 3 2 Mass Transfer Coefficients in a
with Structured Packing, 362 * :* *
12 3 4 Transfer Units for Multicomponent Systems, 364^
Example 12 3 3 Distillation of a Quaternary Sy amp;iti
in a Sulzer Packed Column, 365 *?*T •”
: If
4 , t
13 Multicomponent Distillation: Efficiency Models j
13 1 Introduction, 371
: p l
SsftSIf
U i I
*
13 1 1 Definitions of Efficiency, 371
13 2 Efficiencies of Binary Systems, 373
13 2 1 Point Efficiency for Binary Systems,
CONTENTS xxi
Example 13 2 1 Point Efficiency of
Toluene-Methylcyclohexane, 373
Example 13 2 2 Point Efficiency for the Regeneration
of Triethylene Glycol, 374
13 2 2 Tray Efficiency, 375
13 3 Efficiencies of Multicomponent Systems, 375
13 3 1 Point Efficiency of Multicomponent Systems, 375
Example 13 3 1 Point Efficiency in the Distillation
of the Methanol-l-Propanol-Water System, 376
Example 13 3 2 Point Efficiencies of EthanoI-tert-Butyl
Alcohol-Water System, 378
13 3 3 Tray Efficiency for Multicomponent Systems, 379
Example 13 3 3 Tray Efficiency in the Distillation
of the Methanol-l-Propanol-Water System, 382
13 4 Column Simulation, 384
13 4 1 The Equilibrium Stage Model, 384
13 4 2 Solving the Model Equations, 387
13 5 Simulation and Experimental Results, 388
13 5 1 Two Nonideal Systems at Total Reflux, 389
13 5 2 Industrial Scale Columns, 390
13 5 3 Simulations of Aittamaa, 391
13 5 4 Other Studies, 394
13 5 5 Design Calculations, 394
13 6 Concluding Remarks, 395
14 Multicomponent Distillation: A Nonequilibrium Stage Model 397
14 1 A Nonequilibrium Model, 398
14 1 1 The Conservation Equations, 399
14 1 2 The Rate Equations, 401
14 1 3 The Interface Model, 402
14 1 4 The Hydraulic Equations, 402
14 1 5 Specifications for Nonequilibrium Simulation, 403
14 2 Solving the Model Equations, 403
14 2 1 Variables and Equations for a Nonequilibrium
Stage, 404
14 2 2 Condensers and Reboilers, 405
14 2 3 Equations and Variables for a Multistage Column, 405
14 2 4 Solution of the Model Equations, 406
14 3 Design Studies, 407
Example 14 3 1 Depropanizer Column Design, 407
Example 14 3 2 Extractive Distillation Column
Design, 411
Example 14 3 3 Ethylbenzene-Styrene Distillation
Column Design, 415
Example 14 3 4 Gas Absorption, 419
xxii CONTENTS
14 4 Experimental Studies, 420
14 4 1 Multicomponent Distillation, 420
14 4 2 Extractive Distillation, 421
14 4 3 Alcohol Wash Columns, 422
14 44A Packed C4 Splitter, 430
14 4 5 Other Applications, 432
14 5 Concluding Remarks—Nonequilibrium or Equilibrium
Model? 434
15 Condensation of Vapor Mixtures 435
15 1 Mass and Energy Transfer in Condensation, 435
15 1 1 Condensation Flow Patterns, 435
15 1 2 Mass and Energy Transfer, 437
15 1 3 Computation of the Fluxes in Multicomponent
Systems, 440
Example 15 1 1 Condensation of a Methanol-Water
Mixture, 442
Example 15 1 2 Condensation of a Binary Vapor in the
Presence of an Inert Gas, 448
15 1 4 Condensation of a Binary Vapor Mixture, 457
15 1 5 Condensation of a Single Vapor in the Presence
of an Inert Gas, 458
Example 15 1 3 Condensation of a Methanol in the
Presence of Nitrogen, 458
15 2 Condenser Design, 461
15 2 1 Material Balance Relations, 462
15 2 2 Energy Balance Relations, 463
15 2 3 Solving the Model Equations, 464
15 3 Design Studies, 465
15 3 1 Example Specifications, 465
15 3 2 Significance of Interaction Effects, 466
15 3 3 Liquid-Phase Models, 470
15 4 Experimental Studies, 471
15 4 1 Multicomponent Condensation, 471
15 4 2 Ternary Mass Transfer in a Wetted Wall Column, 473
15 5 Conclusions and Recommendations, 476
Postface 478
Exercises 480
CONTENTS xxiii
Appendix A
Appendix B
Appendix C
Appendix D
Review of Matrix Analysis 506
A 1 Introduction, 506
A11 Definition, 506
A12 Principal Types of Matrix, 507
A 2 Elementary Operations and Properties
of Matrices, 508
A21 Addition, 509
A22 Multiplication by a Scalar, 509
A23 Multiplication of Two Matrices, 509
A24 Differentiation and Integration
of Matrices, 511
A3 The Inverse, 512
A31 Properties of the Inverse and Transpose, 513
A 4 Eigenvalues and Eigenvectors, 514
A41 Properties of Eigenvalues, 515
A42 Eigenvectors, 516
A43 Similar Matrices, 516
A44 Diagonalizable Matrices, 516
A 5 Matrix Calculus, 517
A51 The Cayley-Hamilton Theorem, 518
A52 Functions of a Matrix, 520
A53 Functions of Diagonalizable Matrices, 520
A 6 Matrix Computations, 522
A61 Arithmetic Operations, 522
A62 Matrix Functions, 522
Solution of Systems of Differential Equations 524
B l Generalization of the Solutions of Scalar Differential
Equations, 524
B 2 The Method of Successive Substitution, 525
B 3 Solution of Coupled Differential Equations
Using Similarity Transformations, 529
Solution of Systems of Algebraic Equations 531
C l Solutions of Systems of Linear Equations, 531
C 2 Solutions of Systems of Nonlinear Equations, 532
C21 Repeated Substitution, 532
C22 Newton’s Method, 532
Estimation of Thermodynamic Factors from Activity
Coefficient Models 534
D l Thermodynamic Factors for Binary Systems, 534
xxiv CONTENTS
D 2 Thermodynamic Factors for Multicomponent
Systems, 542
D 3 Thermodynamic Fluid Stability and the Gibbs Free
Energy, 548
Appendix E About the Software 549
E l
E 2
E 3
E 4
E 5
E 6
What is on This Disk, 549
Hardware Requirements, 549
What is Mathcad?, 550
Making a Backup Copy, 550
Installing the Disk, 551
How to Use the Files on this Disk, 552
References 555
Author Index 571
Subject Index 575
|
any_adam_object | 1 |
author | Taylor, Ross 1954- Krishna, Rajamani |
author_GND | (DE-588)174091699 |
author_facet | Taylor, Ross 1954- Krishna, Rajamani |
author_role | aut aut |
author_sort | Taylor, Ross 1954- |
author_variant | r t rt r k rk |
building | Verbundindex |
bvnumber | BV010114067 |
callnumber-first | T - Technology |
callnumber-label | TP156 |
callnumber-raw | TP156.M3 |
callnumber-search | TP156.M3 |
callnumber-sort | TP 3156 M3 |
callnumber-subject | TP - Chemical Technology |
classification_rvk | UG 2900 |
classification_tum | MTA 800f CIT 020f |
ctrlnum | (OCoLC)299749687 (DE-599)BVBBV010114067 |
dewey-full | 660.28423 |
dewey-hundreds | 600 - Technology (Applied sciences) |
dewey-ones | 660 - Chemical engineering |
dewey-raw | 660.28423 |
dewey-search | 660.28423 |
dewey-sort | 3660.28423 |
dewey-tens | 660 - Chemical engineering |
discipline | Chemie / Pharmazie Physik Chemie-Ingenieurwesen |
format | Book |
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id | DE-604.BV010114067 |
illustrated | Illustrated |
indexdate | 2024-07-09T17:46:45Z |
institution | BVB |
isbn | 0471574171 9780471574170 |
language | English |
oai_aleph_id | oai:aleph.bib-bvb.de:BVB01-006715961 |
oclc_num | 299749687 |
open_access_boolean | |
owner | DE-91G DE-BY-TUM DE-703 DE-1051 DE-29T DE-634 DE-83 DE-19 DE-BY-UBM |
owner_facet | DE-91G DE-BY-TUM DE-703 DE-1051 DE-29T DE-634 DE-83 DE-19 DE-BY-UBM |
physical | XXXIV, 579 S. graph. Darst. 1 Diskette, 3,5" |
publishDate | 1993 |
publishDateSearch | 1993 |
publishDateSort | 1993 |
publisher | Wiley |
record_format | marc |
series2 | Wiley series in chemical engineering |
spelling | Taylor, Ross 1954- Verfasser (DE-588)174091699 aut Multicomponent mass transfer Ross Taylor ; R. Krishna New York [u.a.] Wiley 1993 XXXIV, 579 S. graph. Darst. 1 Diskette, 3,5" txt rdacontent n rdamedia nc rdacarrier Wiley series in chemical engineering Hier auch später erschienene, unveränderte Nachdrucke Stoffübertragung (DE-588)4057696-6 gnd rswk-swf Mehrstoffsystem (DE-588)4132152-2 gnd rswk-swf Stoffübertragung (DE-588)4057696-6 s Mehrstoffsystem (DE-588)4132152-2 s DE-604 Krishna, Rajamani Verfasser aut HEBIS Datenaustausch application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=006715961&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA Inhaltsverzeichnis |
spellingShingle | Taylor, Ross 1954- Krishna, Rajamani Multicomponent mass transfer Stoffübertragung (DE-588)4057696-6 gnd Mehrstoffsystem (DE-588)4132152-2 gnd |
subject_GND | (DE-588)4057696-6 (DE-588)4132152-2 |
title | Multicomponent mass transfer |
title_auth | Multicomponent mass transfer |
title_exact_search | Multicomponent mass transfer |
title_full | Multicomponent mass transfer Ross Taylor ; R. Krishna |
title_fullStr | Multicomponent mass transfer Ross Taylor ; R. Krishna |
title_full_unstemmed | Multicomponent mass transfer Ross Taylor ; R. Krishna |
title_short | Multicomponent mass transfer |
title_sort | multicomponent mass transfer |
topic | Stoffübertragung (DE-588)4057696-6 gnd Mehrstoffsystem (DE-588)4132152-2 gnd |
topic_facet | Stoffübertragung Mehrstoffsystem |
url | http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=006715961&sequence=000001&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA |
work_keys_str_mv | AT taylorross multicomponentmasstransfer AT krishnarajamani multicomponentmasstransfer |