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ویرایش: نویسندگان: Doğu T., Doğu G. سری: ISBN (شابک) : 9781119755890 ناشر: John Wiley & Sons سال نشر: 2022 تعداد صفحات: 345 [346] زبان: English فرمت فایل : PDF (درصورت درخواست کاربر به PDF، EPUB یا AZW3 تبدیل می شود) حجم فایل: 9 Mb
در صورت تبدیل فایل کتاب Fundamentals of Chemical Reactor Engineering: A Multi-Scale Approach به فرمت های PDF، EPUB، AZW3، MOBI و یا DJVU می توانید به پشتیبان اطلاع دهید تا فایل مورد نظر را تبدیل نمایند.
توجه داشته باشید کتاب مبانی مهندسی راکتور شیمیایی: یک رویکرد چند مقیاسی نسخه زبان اصلی می باشد و کتاب ترجمه شده به فارسی نمی باشد. وبسایت اینترنشنال لایبرری ارائه دهنده کتاب های زبان اصلی می باشد و هیچ گونه کتاب ترجمه شده یا نوشته شده به فارسی را ارائه نمی دهد.
Cover Half Title Fundamentals of Chemical Reactor Engineering: A Multi-Scale Approach Copyright Dedication Contents Preface Foreword Foreword 2 About the Authors and Acknowledgments List of Symbols About the Companion Website 1. Rate Concept and Species Conservation Equations in Reactors 1.1 Reaction Rates of Species in Chemical Conversions 1.2 Rate of a Chemical Change 1.3 Chemical Reactors and Conservation of Species 1.4 Flow Reactors and the Reaction Rate Relations 1.5 Comparison of Perfectly Mixed Flow and Batch Reactors 1.6 Ideal Tubular Flow Reactor 1.7 Stoichiometric Relations Between Reacting Species 1.7.1 Batch Reactor Analysis 1.7.2 Steady-Flow Analysis for a CSTR 1.7.3 Unsteady Perfectly Mixed-Flow Reactor Analysis Problems and Questions References 2. Reversible Reactions and Chemical Equilibrium 2.1 Equilibrium and Reaction Rate Relations 2.2 Thermodynamics of Chemical Reactions 2.3 Different Forms of Equilibrium Constant 2.4 Temperature Dependence of Equilibrium Constant and Equilibrium Calculations Problems and Questions References 3. Chemical Kinetics and Analysis of Batch Reactors 3.1 Kinetics and Mechanisms of Homogeneous Reactions 3.2 Batch Reactor Data Analysis 3.2.1 Integral Method of Analysis 3.2.1.1 First-Order Reaction 3.2.1.2 nth-Order Reaction and Method of Half-Lives 3.2.1.3 Overall Second-Order Reaction Between Reactants A and B 3.2.1.4 Second-Order Autocatalytic Reactions 3.2.1.5 Zeroth-Order Dependence of Reaction Rate on Concentrations 3.2.1.6 Data Analysis for a Reversible Reaction 3.2.2 Differential Method of Data Analysis 3.3 Changes in Total Pressure or Volume in Gas-Phase Reactions Problems and Questions References 4. Ideal-Flow Reactors: CSTR and Plug-Flow Reactor Models 4.1 CSTR Model 4.1.1 CSTR Data Analysis 4.2 Analysis of Ideal Plug-Flow Reactor 4.3 Comparison of Performances of CSTR and Ideal Plug-Flow Reactors 4.4 Equilibrium and Rate Limitations in Ideal-Flow Reactors 4.5 Unsteady Operation of Reactors 4.5.1 Unsteady Operation of a Constant Volume Stirred-Tank Reactor 4.5.2 Semi-batch Reactors 4.6 Analysis of a CSTR with a Complex Rate Expression Problems and Questions References 5. Multiple Reactor Systems 5.1 Multiple CSTRs Operating in Series 5.1.1 Graphical Method for Multiple CSTRs 5.2 Multiple Plug-Flow Reactors Operating in Series 5.3 CSTR and Plug-Flow Reactor Combinations Problems and Questions References 6. Multiple Reaction Systems 6.1 Selectivity and Yield Definitions 6.2 Selectivity Relations for Ideal Flow Reactors 6.3 Design of Ideal Reactors and Product Distributions for Multiple Reaction Systems 6.3.1 Parallel Reactions 6.3.2 Consecutive Reactions Problems and Questions References 7. Heat Effects and Non-isothermal Reactor Design 7.1 Heat Effects in a Stirred-Tank Reactor 7.2 Steady-State Multiplicity in a CSTR 7.3 One-Dimensional Energy Balance for a Tubular Reactor 7.4 Heat Effects in Multiple Reaction Systems 7.4.1 Heat Effects in a CSTR with Parallel Reactions 7.4.2 Heat Effects in a CSTR with Consecutive Reactions 7.4.3 Energy Balance for a Plug-Flow Reactor with Multiple Reactions 7.5 Heat Effects in Multiple Reactors and Reversible Reactions 7.5.1 Temperature Selection and Multiple Reactor Combinations 7.5.1.1 Endothermic-Reversible Reactions in a Multi-stage Reactor System 7.5.2 Cold Injection Between Reactors 7.5.3 Heat-Exchanger Reactors Problems and Questions Case Studies References 8. Deviations from Ideal Reactor Performance 8.1 Residence Time Distributions in Flow Reactors 8.2 General Species Conservation Equation in a Reactor 8.3 Laminar Flow Reactor Model 8.4 Dispersion Model for a Tubular Reactor 8.5 Prediction of Axial Dispersion Coefficient 8.6 Evaluation of Dispersion Coefficient by Moment Analysis 8.7 Radial Temperature Variations in Tubular Reactors 8.8 A Criterion for the Negligible Effect of Radial Temperature Variations on the Reaction Rate 8.9 Effect of L/dt Ratio on the Performance of a Tubular Reactor and Pressure Drop Problems and Questions Exercises References 9. Fixed-Bed Reactors and Interphase Transport Effects 9.1 Solid-Catalyzed Reactions and Transport Effects Within Reactors 9.2 Observed Reaction Rate and Fixed-Bed Reactors 9.3 Significance of Film Mass Transfer Resistance in Catalytic Reactions 9.4 Tubular Reactors with Catalytic Walls 9.4.1 One-Dimensional Model 9.4.2 Two-Dimensional Model 9.5 Modeling of a Non-isothermal Fixed-Bed Reactor 9.6 Steady-State Multiplicity on the Surface of a Catalyst Pellet Exercises References 10. Transport Effects and Effectiveness Factor for Reactions in Porous Catalysts 10.1 Effectiveness Factor Expressions in an Isothermal Catalyst Pellet 10.2 Observed Activation Energy and Observed Reaction Order 10.3 Effectiveness Factor in the Presence of Pore-Diffusion and Film Mass Transfer Resistances 10.4 Thermal Effects in Porous Catalyst Pellets 10.5 Interphase and Intrapellet Temperature Gradients for Catalyst Pellets 10.6 Pore Structure Optimization and Effectiveness Factor Analysis for Catalysts with Bi-modal Pore-Size Distributions 10.7 Criteria for Negligible Transport Effects in Catalytic Reactions 10.7.1 Criteria for Negligible Diffusion and Heat Effects on the Observed Rate of Solid-Catalyzed Reactions 10.7.2 Relative Importance of Concentration and Temperature Gradients in Catalyst Pellets 10.7.3 Intrapellet and External Film Transport Limitations 10.7.4 A Criterion for Negligible Diffusion Resistance in Bidisperse Catalyst Pellets 10.8 Transport Effects on Product Selectivities in Catalytic Reactions 10.8.1 Film Mass Transfer Effect 10.8.2 Pore-Diffusion Effect Problems and Questions Exercises References 11. Introduction to Catalysis and Catalytic Reaction Mechanisms 11.1 Basic Concepts in Heterogeneous Catalysis 11.2 Surface Reaction Mechanisms 11.3 Adsorption Isotherms 11.4 Deactivation of Solid Catalysts Exercises References 12. Diffusion in Porous Catalysts 12.1 Diffusion in a Capillary 12.2 Effective Diffusivities in Porous Solids 12.3 Surface Diffusion 12.4 Models for the Prediction of Effective Diffusivities 12.4.1 Random Pore Model 12.4.2 Grain Model 12.5 Diffusion and Flow in Porous Solids 12.6 Experimental Methods for the Evaluation of Effective Diffusion Coefficients 12.6.1 Steady-State Methods 12.6.2 Dynamic Methods 12.6.3 Single-Pellet Moment Method Exercises References 13. Process Intensification and Multifunctional Reactors 13.1 Membrane Reactors 13.1.1 Modeling of a Membrane Reactor 13.1.2 General Conservation Equations and Heat Effects in a Membrane Reactor 13.2 Reactive Distillation 13.2.1 Equilibrium-Stage Model 13.2.2 A Rate-Based Model for a Continuous Reactive Distillation Column 13.3 Sorption-Enhanced Reaction Process 13.4 Monolithic and Microchannel Reactors 13.4.1 Microchannel Reactors 13.5 Chromatographic Reactors 13.6 Alternative Energy Sources for Chemical Processing 13.6.1 Microwave-Assisted Chemical Conversions 13.6.2 Ultrasound Reactors 13.6.3 Solar Energy for Chemical Conversion References 14. Multiphase Reactors 14.1 Slurry Reactors 14.2 Trickle-Bed Reactors 14.3 Fluidized-Bed Reactors References 15. Kinetics and Modeling of Non-catalytic Gas–Solid Reactions 15.1 Unreacted-Core Model 15.2 Deactivation and Structural Models for Gas–Solid Reactions 15.3 Chemical Vapor Deposition Reactors Exercises References Appendix A. Some Constants of Nature Appendix B. Conversion Factors Appendix C. Dimensionless Groups and Parameters Index