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Preface | p. xiii |
To the Student | p. xv |
Acknowledgments | p. xix |
Instructors' and Readers' Guide | p. xxi |
Introduction | p. 3 |
References | p. 19 |
Chemical Reactor Analysis | p. 20 |
The Batch Reactor | p. 21 |
Chemical Equilibrium | p. 25 |
Reaction Rate and Determination by Experiment | p. 26 |
Rate Expression | p. 26 |
Approach to Equilibrium | p. 32 |
Tank-Type Reactors | p. 33 |
Batch Reactors | p. 34 |
Semibatch Reactors | p. 34 |
Continuous Flow | p. 37 |
Tubular Reactors | p. 42 |
Reactor Energy Balance | p. 47 |
References | p. 51 |
Problems | p. 51 |
Heat Exchanger Analysis | p. 55 |
Batch Heat Exchangers | p. 56 |
Level I Analysis | p. 57 |
Level II Thermal Equilibrium | p. 58 |
Rate of Heat Transfer and Determination by Experiment | p. 60 |
Rate Expression | p. 61 |
Approach to Equilibrium | p. 65 |
Tank-Type Heat Exchangers | p. 67 |
Batch Heat Exchanger | p. 68 |
Semibatch Heat Exchanger | p. 68 |
Mixed-Mixed Fluid Motions | p. 69 |
Mixed-Plug Fluid Motions | p. 72 |
Continuous-Flow Tank-Type Heat Exchangers | p. 74 |
Mixed-Mixed Fluid Motions | p. 74 |
Mixed-Plug Fluid Motions | p. 78 |
Tubular Heat Exchangers | p. 79 |
Cocurrent Flow | p. 81 |
Countercurrent Flow-Double-Pipe Heat Exchanger | p. 88 |
Technically Feasible Heat Exchanger Design | p. 94 |
Design Procedure | p. 96 |
References | p. 102 |
Problems | p. 103 |
Energy Balance | p. 109 |
Mass Contactor Analysis | p. 114 |
Batch Mass Contactors | p. 118 |
Level I Analysis | p. 119 |
Level II Analysis, Phase Equilibrium | p. 120 |
Rate of Mass Transfer and Determination by Experiment | p. 125 |
Rate Expression | p. 127 |
Approach to Equilibrium | p. 132 |
Tank-Type Two-Phase Mass Contactors | p. 134 |
Batch Mass Contactors | p. 135 |
Semibatch Mass Contactors | p. 137 |
Mixed-Mixed Fluid Motions | p. 138 |
Mixed-Plug Fluid Motions | p. 139 |
Continuous-Flow Two-Phase Mass Contactors | p. 143 |
Mixed-Mixed Fluid Motions | p. 144 |
Design of a Continuous Mixed-Mixed Mass Contactor | p. 146 |
Mixed-Plug Fluid Motions | p. 153 |
Tubular Two-Phase Mass Contactors | p. 156 |
Cocurrent Flow | p. 158 |
Countercurrent Flow | p. 159 |
Gas-Liquid Countercurrent Contactors | p. 164 |
Continuous-Flow Mass Contactor Design Summary | p. 168 |
References | p. 175 |
Problems | p. 175 |
"Log-Mean" Concentration Difference | p. 178 |
Equivalence Between Heat and Mass Transfer Model Equations | p. 180 |
Nomenclature for Part I | p. 181 |
Conduction and Diffusion | p. 187 |
Rate of Thermal Conduction | p. 187 |
Experimental Determination of Thermal Conductivity k and Verification of Fourier's Constitutive Equation | p. 187 |
Definition of the Biot Number for Heat Transfer | p. 195 |
Definition of the Nusselt Number | p. 199 |
Rate of Molecular Diffusion | p. 201 |
Experimental Determination of Binary Diffusivities D[subscript AB] and Verification of Fick's Constitutive Equation | p. 201 |
Definition of the Biot Number for Mass Transfer | p. 206 |
Definition of the Sherwood Number | p. 208 |
Geometric Effects on Steady Heat Conduction and Diffusion in Solids and Quiescent Fluids | p. 209 |
One-Dimensional Heat Conduction in Nonplanar Geometries | p. 209 |
One-Dimensional Diffusion in a Conical Geometry | p. 211 |
Conduction and Diffusion Through Composite Layered Materials in Series | p. 212 |
Overall Heat Transfer Coefficient for Composite Walls: Resistance Formulation | p. 212 |
Overall Heat Transfer Coefficient for a Tubular Exchanger | p. 217 |
Overall Mass Transfer Coefficient for Diffusion Through a Composite Wall | p. 220 |
Molecular Conduction and Diffusion with Generation | p. 222 |
Radial Heat Conduction with Generation | p. 222 |
Diffusion with Chemical Reaction | p. 224 |
Diffusion-Induced Convection: The Arnold Cell | p. 225 |
Basics of Membrane Diffusion: The Sorption-Diffusion Model | p. 230 |
Transient Conduction and Diffusion | p. 231 |
Short-Time Penetration Solution | p. 233 |
Small Biot Numbers-Lumped Analysis | p. 235 |
Nomenclature | p. 236 |
Important Dimensionless Groups | p. 238 |
References | p. 239 |
Problems | p. 240 |
Convective Heat and Mass Transfer | p. 246 |
The Differential Transport Equations for Fluids with Constant Physical Properties in a Laminar Boundary Layer | p. 247 |
Mass Conservation-Continuity Equation | p. 248 |
Momentum Transport-Navier-Stokes Equation | p. 249 |
Energy Conservation | p. 250 |
Species Mass Conservation | p. 252 |
Boundary-Layer Analysis and Transport Analogies | p. 254 |
Laminar Boundary Layer | p. 254 |
Reynolds Transport Analogy | p. 257 |
Effects of Material Properties: The Chilton-Colburn Analogy | p. 260 |
Turbulent Boundary Layers | p. 263 |
Transport Correlations for Specific Geometries | p. 264 |
Models for Estimating Transport Coefficients in Fluid-Fluid Systems | p. 273 |
Film Theory | p. 273 |
Penetration Theory | p. 273 |
Surface Renewal Theory | p. 278 |
Interphase Mass Transfer | p. 279 |
Summary of Convective Transport Coefficient Estimations | p. 281 |
Heat Exchangers | p. 281 |
Mass Contactors | p. 284 |
Nomenclature | p. 286 |
References | p. 287 |
Problems | p. 287 |
Derivation of the Transport Equations | p. 293 |
Vector Notation | p. 299 |
Estimation of the Mass Transfer Coefficient and Interfacial Area in Fluid-Fluid Mass Contactors | p. 301 |
Estimation of Bubble and Drop Size | p. 304 |
Tank-Type Mass Contactors | p. 307 |
Mixed-Mixed Interfacial Area Estimation | p. 307 |
Mixed-Mixed K[subscript m] Estimation | p. 309 |
Mixed-Plug Area Estimation | p. 309 |
Mixed-Plug K[subscript m] Estimation | p. 313 |
Tubular Contactors | p. 316 |
Cocurrent Area Estimation | p. 316 |
Cocurrent K[subscript m] Estimation | p. 318 |
Countercurrent Area Estimation | p. 318 |
Countercurrent K[subscript m] Estimation | p. 320 |
Nomenclature | p. 320 |
References | p. 321 |
Problems | p. 322 |
Bubble and Drop Breakage | p. 323 |
Technically Feasible Design Case Studies | p. 327 |
Technically Feasible Design of a Heat Exchanger | p. 328 |
Technically Feasible Design of a Countercurrent Mass Contactor | p. 335 |
Analysis of a Pilot-Scale Bioreactor | p. 345 |
Nomenclature | p. 353 |
References | p. 354 |
Problems | p. 354 |
Index | p. 363 |
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