Coulson and Richardson's chemical engineering. Volume 3A, Chemical and biochemical reactors and reaction engineering /
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| Edition: | Fourth edition. |
|---|---|
| Imprint: | Kidlington, Oxford, United Kingdom : Butterworth-Heinemann is an imprint of Elsevier, 2017. |
| Description: | 1 online resource. |
| Language: | English |
| Subject: | |
| Format: | E-Resource Book |
| URL for this record: | http://pi.lib.uchicago.edu/1001/cat/bib/11361710 |
Table of Contents:
- Front Cover; Coulson and Richardson's Chemical Engineering; Coulson and Richardson's Chemical Engineering: Volume 3A: Chemical and Biochemical Reactors and Reaction Engineering; Copyright; Contents; List of Contributors; Preface; 1
- Reactor Design-General Principles; 1.1 Basic Objectives in Design of a Reactor; 1.1.1 By-products and Their Economic Importance; 1.1.2 Preliminary Appraisal of a Reactor Project; 1.2 Classification of Reactors and Choice of Reactor Type; 1.2.1 Homogeneous and Heterogeneous Reactors; 1.2.2 Batch Reactors and Continuous Reactors
- 1.2.3 Variations in Contacting Pattern-Semibatch Operation1.2.4 Influence of Heat of Reaction on Reactor Type; 1.2.4.1 Adiabatic Reactors; 1.2.4.2 Reactors With Heat Transfer; 1.2.4.3 Autothermal Reactor Operation; 1.3 Choice of Process Conditions; 1.3.1 Chemical Equilibria and Chemical Kinetics; 1.3.2 Calculation of Equilibrium Conversion; 1.3.3 Ultimate Choice of Reactor Conditions; 1.4 Material and Energy Balances; 1.4.1 Material Balance and the Concept of Rate of Generation of a Species; 1.4.2 Energy Balance; 1.5 Chemical Kinetics and Rate Equations
- 1.5.1 Definition of Order of Reaction and Rate Constant1.5.2 Influence of Temperature: Activation Energy; 1.5.3 Rate Equations and Reaction Mechanism; 1.5.4 Reversible Reactions; 1.5.5 Experimental Determination of Kinetic Constants; 1.6 Batch Reactors; 1.6.1 Calculation of Reaction Time: Basic Design Equation; 1.6.2 Reaction Time-Isothermal Operation; 1.6.3 Maximum Production Rate; 1.6.4 Reaction Time-Nonisothermal Operation; 1.6.5 Adiabatic Operation; 1.6.6 Kinetics From Batch Reactor Data; 1.6.6.1 Differential Method; 1.6.6.2 Integral Method
- 1.6.6.3 Differential Versus Integral Method: Comparison1.6.6.4 Fractional Life Method; 1.6.6.5 Kinetics of Gas-Phase Reactions From Pressure Measurements; 1.7 Tubular Flow Reactors; 1.7.1 Basic Design Equations for a Tubular Reactor; 1.7.2 Tubular Reactors-Nonisothermal Operation; 1.7.3 Pressure Drop in Tubular Reactors; 1.7.4 Kinetic Data From Tubular Reactors; 1.8 Continuous Stirred Tank Reactors; 1.8.1 Assumption of Ideal Mixing: Residence Time; 1.8.2 Design Equations for Continuous Stirred Tank Reactors; 1.8.3 Graphical Methods; 1.8.4 Autothermal Operation
- 1.8.5 Kinetic Data From Continuous Stirred Tank Reactors1.9 Comparison of Batch, Tubular, and Stirred Tank Reactors for a Single Reaction: Reactor Output; 1.9.1 Batch Reactor and Tubular Plug Flow Reactor; 1.9.2 Continuous Stirred Tank Reactor; 1.9.2.1 One Tank; 1.9.2.2 Two Tanks; 1.9.3 Comparison of Reactors; 1.10 Comparison of Batch, Tubular, and Stirred Tank Reactors for Multiple Reactions: Reactor Yield; 1.10.1 Types of Multiple Reactions; 1.10.2 Yield and Selectivity; 1.10.3 Reactor Type and Backmixing; 1.10.4 Reactions in Parallel; 1.10.4.1 Requirements for High Yield