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Preface | |
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To the Student | |
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Acknowledgments | |
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Instructors' and Readers' Guide | |
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Introduction | |
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References | |
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Chemical Reactor Analysis | |
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The Batch Reactor | |
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Chemical Equilibrium | |
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Reaction Rate and Determination by Experiment | |
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Rate Expression | |
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Approach to Equilibrium | |
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Tank-Type Reactors | |
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Batch Reactors | |
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Semibatch Reactors | |
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Continuous Flow | |
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Tubular Reactors | |
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Reactor Energy Balance | |
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References | |
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Problems | |
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Heat Exchanger Analysis | |
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Batch Heat Exchangers | |
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Level I Analysis | |
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Level II Thermal Equilibrium | |
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Rate of Heat Transfer and Determination by Experiment | |
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Rate Expression | |
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Approach to Equilibrium | |
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Tank-Type Heat Exchangers | |
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Batch Heat Exchanger | |
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Semibatch Heat Exchanger | |
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Mixed-Mixed Fluid Motions | |
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Mixed-Plug Fluid Motions | |
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Continuous-Flow Tank-Type Heat Exchangers | |
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Mixed-Mixed Fluid Motions | |
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Mixed-Plug Fluid Motions | |
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Tubular Heat Exchangers | |
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Cocurrent Flow | |
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Countercurrent Flow-Double-Pipe Heat Exchanger | |
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Technically Feasible Heat Exchanger Design | |
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Design Procedure | |
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References | |
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Problems | |
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Energy Balance | |
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Mass Contactor Analysis | |
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Batch Mass Contactors | |
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Level I Analysis | |
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Level II Analysis, Phase Equilibrium | |
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Rate of Mass Transfer and Determination by Experiment | |
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Rate Expression | |
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Approach to Equilibrium | |
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Tank-Type Two-Phase Mass Contactors | |
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Batch Mass Contactors | |
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Semibatch Mass Contactors | |
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Mixed-Mixed Fluid Motions | |
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Mixed-Plug Fluid Motions | |
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Continuous-Flow Two-Phase Mass Contactors | |
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Mixed-Mixed Fluid Motions | |
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Design of a Continuous Mixed-Mixed Mass Contactor | |
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Mixed-Plug Fluid Motions | |
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Tubular Two-Phase Mass Contactors | |
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Cocurrent Flow | |
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Countercurrent Flow | |
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Gas-Liquid Countercurrent Contactors | |
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Continuous-Flow Mass Contactor Design Summary | |
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References | |
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Problems | |
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"Log-Mean" Concentration Difference | |
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Equivalence Between Heat and Mass Transfer Model Equations | |
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Nomenclature for Part I | |
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Conduction and Diffusion | |
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Rate of Thermal Conduction | |
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Experimental Determination of Thermal Conductivity k and Verification of Fourier's Constitutive Equation | |
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Definition of the Biot Number for Heat Transfer | |
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Definition of the Nusselt Number | |
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Rate of Molecular Diffusion | |
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Experimental Determination of Binary Diffusivities D[subscript AB] and Verification of Fick's Constitutive Equation | |
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Definition of the Biot Number for Mass Transfer | |
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Definition of the Sherwood Number | |
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Geometric Effects on Steady Heat Conduction and Diffusion in Solids and Quiescent Fluids | |
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One-Dimensional Heat Conduction in Nonplanar Geometries | |
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One-Dimensional Diffusion in a Conical Geometry | |
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Conduction and Diffusion Through Composite Layered Materials in Series | |
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Overall Heat Transfer Coefficient for Composite Walls: Resistance Formulation | |
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Overall Heat Transfer Coefficient for a Tubular Exchanger | |
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Overall Mass Transfer Coefficient for Diffusion Through a Composite Wall | |
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Molecular Conduction and Diffusion with Generation | |
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Radial Heat Conduction with Generation | |
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Diffusion with Chemical Reaction | |
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Diffusion-Induced Convection: The Arnold Cell | |
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Basics of Membrane Diffusion: The Sorption-Diffusion Model | |
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Transient Conduction and Diffusion | |
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Short-Time Penetration Solution | |
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Small Biot Numbers-Lumped Analysis | |
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Nomenclature | |
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Important Dimensionless Groups | |
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References | |
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Problems | |
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Convective Heat and Mass Transfer | |
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The Differential Transport Equations for Fluids with Constant Physical Properties in a Laminar Boundary Layer | |
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Mass Conservation-Continuity Equation | |
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Momentum Transport-Navier-Stokes Equation | |
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Energy Conservation | |
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Species Mass Conservation | |
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Boundary-Layer Analysis and Transport Analogies | |
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Laminar Boundary Layer | |
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Reynolds Transport Analogy | |
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Effects of Material Properties: The Chilton-Colburn Analogy | |
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Turbulent Boundary Layers | |
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Transport Correlations for Specific Geometries | |
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Models for Estimating Transport Coefficients in Fluid-Fluid Systems | |
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Film Theory | |
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Penetration Theory | |
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Surface Renewal Theory | |
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Interphase Mass Transfer | |
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Summary of Convective Transport Coefficient Estimations | |
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Heat Exchangers | |
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Mass Contactors | |
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Nomenclature | |
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References | |
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Problems | |
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Derivation of the Transport Equations | |
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Vector Notation | |
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Estimation of the Mass Transfer Coefficient and Interfacial Area in Fluid-Fluid Mass Contactors | |
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Estimation of Bubble and Drop Size | |
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Tank-Type Mass Contactors | |
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Mixed-Mixed Interfacial Area Estimation | |
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Mixed-Mixed K[subscript m] Estimation | |
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Mixed-Plug Area Estimation | |
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Mixed-Plug K[subscript m] Estimation | |
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Tubular Contactors | |
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Cocurrent Area Estimation | |
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Cocurrent K[subscript m] Estimation | |
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Countercurrent Area Estimation | |
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Countercurrent K[subscript m] Estimation | |
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Nomenclature | |
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References | |
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Problems | |
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Bubble and Drop Breakage | |
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Technically Feasible Design Case Studies | |
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Technically Feasible Design of a Heat Exchanger | |
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Technically Feasible Design of a Countercurrent Mass Contactor | |
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Analysis of a Pilot-Scale Bioreactor | |
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Nomenclature | |
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References | |
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Problems | |
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Index | |