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Informationen zum Autor Dr. Gilbert F. Froment is Professor Emeritus of Chemical Engineering at the University of Gent, Belgium, and Research Professor of Texas A&M University. Kenneth B. Bischoff is the author of Chemical Reactor Analysis and Design, 3rd Edition, published by Wiley. Klappentext This is the Third Edition of the standard text on chemical reaction engineering, beginning with basic definitions and fundamental principles and continuing all the way to practical applications, emphasising real-world aspects of industrial practice. The two main sections cover applied or engineering kinetics, reactor analysis and design. Includes updated coverage of computer modeling methods and many new worked examples. Most of the examples use real kinetic data from processes of industrial importance. Zusammenfassung This is the Third Edition of the standard text on chemical reaction engineering, beginning with basic definitions and fundamental principles and continuing all the way to practical applications, emphasising real-world aspects of industrial practice. The two main sections cover applied or engineering kinetics, reactor analysis and design. Inhaltsverzeichnis Chapter 1: Elements of Reaction Kinetics.1.1 Definitions of Chemical Rates.1.2 Rate Equations.1.3 Coupled Reactions.1.4 Reducing the Size of Kinetic Models.1.5 Bio-Kinetics.1.6 Complex Reactions.1.7 Modeling the Rate Coefficient.Chapter 2: Kinetics of Heterogeneous Catalytic Reactions.2.1 Introduction.2.2 Adsorption on Solid Catalysts.2.3 Rate Equations.2.4 Complex Catalytic Reactions.2.5 Experimental Reactors.2.6 Model Discrimination and Parameter Estimation.2.7 Sequential Design of Experiments.2.8 Expert Systems in Kinetics Studies.Chapter 3: Transport Processes with Reactions Catalyzed by Solids.Part One Interfacial Gradient Effects.3.1 Reaction of a component of a fluid at the surface of a solid.3.2 Mass and heat transfer resistances.3.3 Concentration or partial pressure and temperature differences.Part Two Intraparticle Gradient Effects.3.4 Molecular-, Knudsen-, and surface diffusion in pores.3.5 Diffusion in a catalyst particle.3.6 Diffusion and reaction in a catalyst particle. A continuum model.3.7 Falsification of rate coefficient and activation energy by diffusion limitations.3.8 Influence of diffusion limitations on the selectivities of coupled reactions.3.9 Criteria for the importance of intraparticle diffusion limitations.3.10 Multiplicity of steady states in catalyst particles.3.11 Combination of external and internal diffusion limitations.3.12 Diagnostic experimental criteria for the absence of internal and external mass transfer limitations.3.13 Nonisothermal particles.Chapter 4: Noncatalytic Gas-Solid Reactions.4.1 A Qualitative Discussion of Gas-Solid Reactions.4.2 General Model with Interfacial and Intraparticle Gradients.4.3 Heterogeneous Model with Shrinking Unreacted Core.4.4 Models Accounting Explicitly for the Structure of the Solid.4.5 On the Use of More Complex Kinetic Equations.Chapter 5: Catalyst Deactivation.5.1 Types of Catalyst Deactivation.5.2 Kinetics of Catalyst Poisoning.5.3 Kinetics of Catalyst Deactivation by Coke Formation.Chapter 6: Gas-Liquid Reactions.6.1 Introduction.6.2 Models for Transfer at a Gas-Liquid Interface.6.3 Two-Film Theory.6.4 Surface Renewal Theory.6.5 Experimental Determination of the Kinetics of Gas-Liquid Reactions.Chapter 7: The Modeling of Chemical Reactors.7.1 Approach.7.2 Aspects of Mass-, Heat- and Momentum Balances.7.3 The Fundamental Model Equations.Chapter 8: The Batch and Semibatch Reactors.Introduction.8.1 The Isothermal Batch Reactor.8.2 The Nonisothermal Batch Reactor.8.3 Semibatch Reactor Modeling.8.4 Optimal Operation Policies and Control Strategies.Chapter 9: The Plug Flow Reactor.9.1 The Continuity, Energy, and Momentum Equations.9.2 ...
