Mass and heat transfer: analysis of mass contactors and heat exchangers
Gespeichert in:
| 1. Verfasser: | |
|---|---|
| Format: | Buch |
| Sprache: | English |
| Veröffentlicht: |
Cambridge [u.a.]
Cambridge Univ. Press
2008
|
| Ausgabe: | 1. publ. |
| Schriftenreihe: | Cambridge series in chemical engineering
|
| Schlagworte: | |
| Online-Zugang: | Contributor biographical information Publisher description Inhaltsverzeichnis Inhaltsverzeichnis |
| Beschreibung: | XXVI, 375 S. Ill., graph. Darst. |
| ISBN: | 9780521886703 |
Internformat
MARC
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| 100 | 1 | |a Russell, Thomas W. Fraser |d 1934- |e Verfasser |0 (DE-588)136262384 |4 aut | |
| 245 | 1 | 0 | |a Mass and heat transfer |b analysis of mass contactors and heat exchangers |c T. W. Fraser Russell ; Anne Skaja Robinson ; Norman J. Wagner |
| 250 | |a 1. publ. | ||
| 264 | 1 | |a Cambridge [u.a.] |b Cambridge Univ. Press |c 2008 | |
| 300 | |a XXVI, 375 S. |b Ill., graph. Darst. | ||
| 336 | |b txt |2 rdacontent | ||
| 337 | |b n |2 rdamedia | ||
| 338 | |b nc |2 rdacarrier | ||
| 490 | 0 | |a Cambridge series in chemical engineering | |
| 650 | 0 | |a Heat exchangers | |
| 650 | 0 | |a Chemical engineering / Equipment and supplies | |
| 650 | 4 | |a Chemical engineering |x Equipment and supplies | |
| 650 | 4 | |a Heat exchangers | |
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Datensatz im Suchindex
| _version_ | 1804137635975790592 |
|---|---|
| adam_text | Contents
Preface page xiii
To the Student xv
Acknowledgments xix
Instructors and Readers Guide xxi
PARTI
1 Introduction 3
References 19
2 Chemical Reactor Analysis 20
2.1 The Batch Reactor 21
2.1.1 Chemical Equilibrium 25
2.2 Reaction Rate and Determination by Experiment 26
2.2.1 Rate Expression 26
2.2.2 Approach to Equilibrium 32
2.3 Tank-Type Reactors 33
2.3.1 Batch Reactors 34
2.3.2 Semibatch Reactors 34
2.3.3 Continuous Flow 37
2.4 Tubular Reactors 42
2.5 Reactor Energy Balance 47
References 51
Problems 51
3 Heat Exchanger Analysis 55
3.1 Batch Heat Exchangers 56
3.1.1 Level I Analysis 57
3.1.2 Level II Thermal Equilibrium 58
3.2 Rate of Heat Transfer and Determination by Experiment 60
3.2.1 Rate Expression 61
3.2.2 Approach to Equilibrium 65
ix
x Contents
3.3 Tank-Type Heat Exchangers 67
3.3.1 Batch Heat Exchanger 68
3.3.2 Semibatch Heat Exchanger 68
3.3.2.1 Mixed-Mixed Fluid Motions 69
3.3.2.2 Mixed-Plug Fluid Motions 72
3.3.3 Continuous-Flow Tank-Type Heat Exchangers 74
3.3.3.1 Mixed-Mixed Fluid Motions 74
3.3.3.2 Mixed-Plug Fluid Motions 78
3.4 Tubular Heat Exchangers 79
3.4.1 Cocurrent Flow 81
3.4.2 Countercurrent Flow—Double-Pipe Heat Exchanger 88
3.5 Technically Feasible Heat Exchanger Design 94
3.5.1 Design Procedure 96
References 102
Problems 103
Appendix. Energy Balance 109
4 Mass Contactor Analysis 114
4.1 Batch Mass Contactors 118
4.1.1 Level I Analysis 119
4.1.2 Level II Analysis, Phase Equilibrium 120
4.2 Rate of Mass Transfer and Determination by Experiment 125
4.2.1 Rate Expression 127
4.2.2 Approach to Equilibrium 132
4.3 Tank-Type Two-Phase Mass Contactors 134
4.3.1 Batch Mass Contactors 135
4.3.2 Semibatch Mass Contactors 137
4.3.2.1 Mixed-Mixed Fluid Motions 138
4.3.2.2 Mixed-Plug Fluid Motions 139
4.3.3 Continuous-Flow Two-Phase Mass Contactors 143
4.3.3.1 Mixed-Mixed Fluid Motions 144
4.3.3.2 Design of a Continuous Mixed-Mixed Mass Contactor 146
4.3.3.3 Mixed-Plug Fluid Motions 153
4.4 Tubular Two-Phase Mass Contactors 156
4.4.1 Cocurrent Flow 158
4.4.2 Countercurrent Flow 159
4.4.3 Gas-Liquid Countercurrent Contactors 164
4.5 Continuous-Flow Mass Contactor Design Summary 168
References 175
Problems 175
Appendix A. Log-Mean Concentration Difference 178
Appendix B. Equivalence Between Heat and Mass Transfer
Model Equations 180
Nomenclature for Part I 181
Contents xi
PART II
5 Conduction and Diffusion 187
5.1 Rate of Thermal Conduction 187
5.1.1 Experimental Determination of Thermal Conductivity k and
Verification of Fourier s Constitutive Equation 187
5.1.2 Definition of the Biot Number for Heat Transfer 195
5.1.3 Definition of the Nusselt Number 199
5.2 Rate of Molecular Diffusion 201
5.2.1 Experimental Determination of Binary Diffusivities DAb and
Verification of Fick s Constitutive Equation 201
5.2.2 Definition of the Biot Number for Mass Transfer 206
5.2.3 Definition of the Sherwood Number 208
5.3 Geometric Effects on Steady Heat Conduction and Diffusion in
Solids and Quiescent Fluids 209
5.3.1 One-Dimensional Heat Conduction in Nonplanar Geometries 209
5.3.2 One-Dimensional Diffusion in a Conical Geometry 211
5.4 Conduction and Diffusion Through Composite Layered Materials
in Series 212
5.4.1 Overall Heat Transfer Coefficient for Composite Walls:
Resistance Formulation 212
5.4.2 Overall Heat Transfer Coefficient for a Tubular Exchanger 217
5.4.3 Overall Mass Transfer Coefficient for Diffusion Through a
Composite Wall 220
5.5 Molecular Conduction and Diffusion with Generation 222
5.5.1 Radial Heat Conduction with Generation 222
5.5.2 Diffusion with Chemical Reaction 224
5.6 Diffusion-Induced Convection: The Arnold Cell 225
5.7 Basics of Membrane Diffusion: The Sorption-Diffusion Model 230
5.8 Transient Conduction and Diffusion 231
5.8.1 Short-Time Penetration Solution 233
5.8.2 Small Biot Numbers—Lumped Analysis 235
Nomenclature 236
Important Dimensionless Groups 238
References 239
Problems 240
6 Convective Heat and Mass Transfer 246
6.1 The Differential Transport Equations for Fluids with Constant
Physical Properties in a Laminar Boundary Layer 247
6.1.1 Mass Conservation—Continuity Equation 248
6.1.2 Momentum Transport—Navier-Stokes Equation 249
6.1.3 Energy Conservation 250
6.1.4 Species Mass Conservation 252
6.2 Boundary-Layer Analysis and Transport Analogies 254
xii Contents
6.2.1 Laminar Boundary Layer 254
6.2.2 Reynolds Transport Analogy 257
6.2.3 Effects of Material Properties: The Chilton-Colburn Analogy 260
6.2.4 Turbulent Boundary Layers 263
6.3 Transport Correlations for Specific Geometries 264
6.4 Models for Estimating Transport Coefficients in Fluid-Fluid Systems 273
6.4.1 Film Theory 273
6.4.2 Penetration Theory 273
6.4.3 Surface Renewal Theory 278
6.4.4 Interphase Mass Transfer 279
6.5 Summary of Convective Transport Coefficient Estimations 281
6.5.1 Heat Exchangers 281
6.5.2 Mass Contactors 284
Nomenclature 286
References 287
Problems 287
Appendix A. Derivation of the Transport Equations 293
Appendix B. Vector Notation 299
7 Estimation of the Mass Transfer Coefficient and Interracial
Area in Fluid-Fluid Mass Contactors 301
7.1 Estimation of Bubble and Drop Size 304
7.2 Tank-Type Mass Contactors 307
7.2.1 Mixed-Mixed Interfacial Area Estimation 307
7.2.2 Mixed-Mixed Km Estimation 309
7.2.3 Mixed-Plug Area Estimation 309
7.2.4 Mixed-Plug Km Estimation 313
7.3 Tubular Contactors 316
7.3.1 Cocurrent Area Estimation 316
7.3.2 Cocurrent Km Estimation 318
7.3.3 Countercurrent Area Estimation 318
7.3.4 Countercurrent Km Estimation 320
Nomenclature 320
References 321
Problems 322
Appendix. Bubble and Drop Breakage 323
8 Technically Feasible Design Case Studies 327
8.1 Technically Feasible Design of a Heat Exchanger 328
8.2 Technically Feasible Design of a Countercurrent Mass Contactor 335
8.3 Analysis of a Pilot-Scale Bioreactor 345
Nomenclature 353
References 354
Problems 354
Index 363
|
| adam_txt |
Contents
Preface page xiii
To the Student xv
Acknowledgments xix
Instructors' and Readers' Guide xxi
PARTI
1 Introduction 3
References 19
2 Chemical Reactor Analysis 20
2.1 The Batch Reactor 21
2.1.1 Chemical Equilibrium 25
2.2 Reaction Rate and Determination by Experiment 26
2.2.1 Rate Expression 26
2.2.2 Approach to Equilibrium 32
2.3 Tank-Type Reactors 33
2.3.1 Batch Reactors 34
2.3.2 Semibatch Reactors 34
2.3.3 Continuous Flow 37
2.4 Tubular Reactors 42
2.5 Reactor Energy Balance 47
References 51
Problems 51
3 Heat Exchanger Analysis 55
3.1 Batch Heat Exchangers 56
3.1.1 Level I Analysis 57
3.1.2 Level II Thermal Equilibrium 58
3.2 Rate of Heat Transfer and Determination by Experiment 60
3.2.1 Rate Expression 61
3.2.2 Approach to Equilibrium 65
ix
x Contents
3.3 Tank-Type Heat Exchangers 67
3.3.1 Batch Heat Exchanger 68
3.3.2 Semibatch Heat Exchanger 68
3.3.2.1 Mixed-Mixed Fluid Motions 69
3.3.2.2 Mixed-Plug Fluid Motions 72
3.3.3 Continuous-Flow Tank-Type Heat Exchangers 74
3.3.3.1 Mixed-Mixed Fluid Motions 74
3.3.3.2 Mixed-Plug Fluid Motions 78
3.4 Tubular Heat Exchangers 79
3.4.1 Cocurrent Flow 81
3.4.2 Countercurrent Flow—Double-Pipe Heat Exchanger 88
3.5 Technically Feasible Heat Exchanger Design 94
3.5.1 Design Procedure 96
References 102
Problems 103
Appendix. Energy Balance 109
4 Mass Contactor Analysis 114
4.1 Batch Mass Contactors 118
4.1.1 Level I Analysis 119
4.1.2 Level II Analysis, Phase Equilibrium 120
4.2 Rate of Mass Transfer and Determination by Experiment 125
4.2.1 Rate Expression 127
4.2.2 Approach to Equilibrium 132
4.3 Tank-Type Two-Phase Mass Contactors 134
4.3.1 Batch Mass Contactors 135
4.3.2 Semibatch Mass Contactors 137
4.3.2.1 Mixed-Mixed Fluid Motions 138
4.3.2.2 Mixed-Plug Fluid Motions 139
4.3.3 Continuous-Flow Two-Phase Mass Contactors 143
4.3.3.1 Mixed-Mixed Fluid Motions 144
4.3.3.2 Design of a Continuous Mixed-Mixed Mass Contactor 146
4.3.3.3 Mixed-Plug Fluid Motions 153
4.4 Tubular Two-Phase Mass Contactors 156
4.4.1 Cocurrent Flow 158
4.4.2 Countercurrent Flow 159
4.4.3 Gas-Liquid Countercurrent Contactors 164
4.5 Continuous-Flow Mass Contactor Design Summary 168
References 175
Problems 175
Appendix A. "Log-Mean" Concentration Difference 178
Appendix B. Equivalence Between Heat and Mass Transfer
Model Equations 180
Nomenclature for Part I 181
Contents xi
PART II
5 Conduction and Diffusion 187
5.1 Rate of Thermal Conduction 187
5.1.1 Experimental Determination of Thermal Conductivity k and
Verification of Fourier's Constitutive Equation 187
5.1.2 Definition of the Biot Number for Heat Transfer 195
5.1.3 Definition of the Nusselt Number 199
5.2 Rate of Molecular Diffusion 201
5.2.1 Experimental Determination of Binary Diffusivities DAb and
Verification of Fick's Constitutive Equation 201
5.2.2 Definition of the Biot Number for Mass Transfer 206
5.2.3 Definition of the Sherwood Number 208
5.3 Geometric Effects on Steady Heat Conduction and Diffusion in
Solids and Quiescent Fluids 209
5.3.1 One-Dimensional Heat Conduction in Nonplanar Geometries 209
5.3.2 One-Dimensional Diffusion in a Conical Geometry 211
5.4 Conduction and Diffusion Through Composite Layered Materials
in Series 212
5.4.1 Overall Heat Transfer Coefficient for Composite Walls:
Resistance Formulation 212
5.4.2 Overall Heat Transfer Coefficient for a Tubular Exchanger 217
5.4.3 Overall Mass Transfer Coefficient for Diffusion Through a
Composite Wall 220
5.5 Molecular Conduction and Diffusion with Generation 222
5.5.1 Radial Heat Conduction with Generation 222
5.5.2 Diffusion with Chemical Reaction 224
5.6 Diffusion-Induced Convection: The Arnold Cell 225
5.7 Basics of Membrane Diffusion: The Sorption-Diffusion Model 230
5.8 Transient Conduction and Diffusion 231
5.8.1 Short-Time Penetration Solution 233
5.8.2 Small Biot Numbers—Lumped Analysis 235
Nomenclature 236
Important Dimensionless Groups 238
References 239
Problems 240
6 Convective Heat and Mass Transfer 246
6.1 The Differential Transport Equations for Fluids with Constant
Physical Properties in a Laminar Boundary Layer 247
6.1.1 Mass Conservation—Continuity Equation 248
6.1.2 Momentum Transport—Navier-Stokes Equation 249
6.1.3 Energy Conservation 250
6.1.4 Species Mass Conservation 252
6.2 Boundary-Layer Analysis and Transport Analogies 254
xii Contents
6.2.1 Laminar Boundary Layer 254
6.2.2 Reynolds Transport Analogy 257
6.2.3 Effects of Material Properties: The Chilton-Colburn Analogy 260
6.2.4 Turbulent Boundary Layers 263
6.3 Transport Correlations for Specific Geometries 264
6.4 Models for Estimating Transport Coefficients in Fluid-Fluid Systems 273
6.4.1 Film Theory 273
6.4.2 Penetration Theory 273
6.4.3 Surface Renewal Theory 278
6.4.4 Interphase Mass Transfer 279
6.5 Summary of Convective Transport Coefficient Estimations 281
6.5.1 Heat Exchangers 281
6.5.2 Mass Contactors 284
Nomenclature 286
References 287
Problems 287
Appendix A. Derivation of the Transport Equations 293
Appendix B. Vector Notation 299
7 Estimation of the Mass Transfer Coefficient and Interracial
Area in Fluid-Fluid Mass Contactors 301
7.1 Estimation of Bubble and Drop Size 304
7.2 Tank-Type Mass Contactors 307
7.2.1 Mixed-Mixed Interfacial Area Estimation 307
7.2.2 Mixed-Mixed Km Estimation 309
7.2.3 Mixed-Plug Area Estimation 309
7.2.4 Mixed-Plug Km Estimation 313
7.3 Tubular Contactors 316
7.3.1 Cocurrent Area Estimation 316
7.3.2 Cocurrent Km Estimation 318
7.3.3 Countercurrent Area Estimation 318
7.3.4 Countercurrent Km Estimation 320
Nomenclature 320
References 321
Problems 322
Appendix. Bubble and Drop Breakage 323
8 Technically Feasible Design Case Studies 327
8.1 Technically Feasible Design of a Heat Exchanger 328
8.2 Technically Feasible Design of a Countercurrent Mass Contactor 335
8.3 Analysis of a Pilot-Scale Bioreactor 345
Nomenclature 353
References 354
Problems 354
Index 363 |
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| index_date | 2024-07-02T20:48:10Z |
| indexdate | 2024-07-09T21:15:26Z |
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| oai_aleph_id | oai:aleph.bib-bvb.de:BVB01-016489565 |
| oclc_num | 180989529 |
| open_access_boolean | |
| owner | DE-703 DE-92 DE-634 |
| owner_facet | DE-703 DE-92 DE-634 |
| physical | XXVI, 375 S. Ill., graph. Darst. |
| publishDate | 2008 |
| publishDateSearch | 2008 |
| publishDateSort | 2008 |
| publisher | Cambridge Univ. Press |
| record_format | marc |
| series2 | Cambridge series in chemical engineering |
| spelling | Russell, Thomas W. Fraser 1934- Verfasser (DE-588)136262384 aut Mass and heat transfer analysis of mass contactors and heat exchangers T. W. Fraser Russell ; Anne Skaja Robinson ; Norman J. Wagner 1. publ. Cambridge [u.a.] Cambridge Univ. Press 2008 XXVI, 375 S. Ill., graph. Darst. txt rdacontent n rdamedia nc rdacarrier Cambridge series in chemical engineering Heat exchangers Chemical engineering / Equipment and supplies Chemical engineering Equipment and supplies Stoffübertragung (DE-588)4057696-6 gnd rswk-swf Wärmeübertragung (DE-588)4064211-2 gnd rswk-swf (DE-588)4173536-5 Patentschrift gnd-content Wärmeübertragung (DE-588)4064211-2 s Stoffübertragung (DE-588)4057696-6 s DE-604 Robinson, Anne Skaja 1966- Sonstige (DE-588)135813468 oth Wagner, Norman Joseph 1962- Sonstige (DE-588)136262392 oth http://www.loc.gov/catdir/enhancements/fy0805/2007045343-b.html Contributor biographical information lizenzfrei http://www.loc.gov/catdir/enhancements/fy0805/2007045343-d.html Publisher description lizenzfrei http://www.loc.gov/catdir/enhancements/fy0805/2007045343-t.html lizenzfrei Inhaltsverzeichnis HBZ Datenaustausch application/pdf http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=016489565&sequence=000002&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA Inhaltsverzeichnis |
| spellingShingle | Russell, Thomas W. Fraser 1934- Mass and heat transfer analysis of mass contactors and heat exchangers Heat exchangers Chemical engineering / Equipment and supplies Chemical engineering Equipment and supplies Stoffübertragung (DE-588)4057696-6 gnd Wärmeübertragung (DE-588)4064211-2 gnd |
| subject_GND | (DE-588)4057696-6 (DE-588)4064211-2 (DE-588)4173536-5 |
| title | Mass and heat transfer analysis of mass contactors and heat exchangers |
| title_auth | Mass and heat transfer analysis of mass contactors and heat exchangers |
| title_exact_search | Mass and heat transfer analysis of mass contactors and heat exchangers |
| title_exact_search_txtP | Mass and heat transfer analysis of mass contactors and heat exchangers |
| title_full | Mass and heat transfer analysis of mass contactors and heat exchangers T. W. Fraser Russell ; Anne Skaja Robinson ; Norman J. Wagner |
| title_fullStr | Mass and heat transfer analysis of mass contactors and heat exchangers T. W. Fraser Russell ; Anne Skaja Robinson ; Norman J. Wagner |
| title_full_unstemmed | Mass and heat transfer analysis of mass contactors and heat exchangers T. W. Fraser Russell ; Anne Skaja Robinson ; Norman J. Wagner |
| title_short | Mass and heat transfer |
| title_sort | mass and heat transfer analysis of mass contactors and heat exchangers |
| title_sub | analysis of mass contactors and heat exchangers |
| topic | Heat exchangers Chemical engineering / Equipment and supplies Chemical engineering Equipment and supplies Stoffübertragung (DE-588)4057696-6 gnd Wärmeübertragung (DE-588)4064211-2 gnd |
| topic_facet | Heat exchangers Chemical engineering / Equipment and supplies Chemical engineering Equipment and supplies Stoffübertragung Wärmeübertragung Patentschrift |
| url | http://www.loc.gov/catdir/enhancements/fy0805/2007045343-b.html http://www.loc.gov/catdir/enhancements/fy0805/2007045343-d.html http://www.loc.gov/catdir/enhancements/fy0805/2007045343-t.html http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&local_base=BVB01&doc_number=016489565&sequence=000002&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA |
| work_keys_str_mv | AT russellthomaswfraser massandheattransferanalysisofmasscontactorsandheatexchangers AT robinsonanneskaja massandheattransferanalysisofmasscontactorsandheatexchangers AT wagnernormanjoseph massandheattransferanalysisofmasscontactorsandheatexchangers |
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Inhaltsverzeichnis