Elemnts Chem Reactn Engr

Cover
 Dedication
 Contents
 Preface
 About the Author
 Chapter 1: Mole Balances
 1.1: The Rate of Reaction, â#x80
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rA
 1.2: The General Mole Balance Equation
 1.3: Batch Reactors (BRs)
 1.4: Continuous-Flow Reactors
 1.4.1: Continuous-Stirred Tank Reactor (CSTR)
 1.4.2: Tubular Reactor
 1.4.3: Packed-Bed Reactor (PBR)
 1.5: Industrial Reactors
 Chapter 2: Conversion and Reactor Sizing
 2.1: Definition of Conversion
 2.2: Batch Reactor Design Equations
 2.3: Design Equations for Flow Reactors
 2.3.1: CSTR (Also Known as a Backmix Reactor or a Vat)
 2.3.2: Tubular Flow Reactor (PFR). 2.3.3: Packed-Bed Reactor (PBR)2.4: Sizing Continuous-Flow Reactors
 2.5: Reactors in Series
 2.5.1: CSTRs in Series
 2.5.2: PFRs in Series
 2.5.3: Combinations of CSTRs and PFRs in Series
 2.5.4: Comparing the CSTR and PFR Reactor Volumes and Reactor Sequencing
 2.6: Some Further Definitions
 2.6.1: Space Time
 2.6.2: Space Velocity
 Chapter 3: Rate Laws
 3.1: Basic Definitions
 3.1.1: Relative Rates of Reaction
 3.2: The Reaction Order and the Rate Law
 3.2.1: Power Law Models and Elementary Rate Laws
 3.2.2: Nonelementary Rate Laws
 3.2.3: Reversible Reactions. 3.3: Rates and the Reaction Rate Constant3.3.1: The Rate Constant k
 3.3.2: The Arrhenius Plot
 3.4: Present Status of Our Approach to Reactor Sizing and Design
 Chapter 4: Stoichiometry
 4.1: Batch Systems
 4.1.1: Batch Concentrations for the Generic Reaction, Equation (2-2)
 4.2: Flow Systems
 4.2.1: Equations for Concentrations in Flow Systems
 4.2.2: Liquid-Phase Concentrations
 4.2.3: Gas-Phase Concentrations
 4.3: Reversible Reactions and Equilibrium Conversion
 Chapter 5: Isothermal Reactor Design: Conversion
 5.1: Design Structure for Isothermal Reactors
 5.2: Batch Reactors (BRs). 5.2.1: Batch Reaction Times5.3: Continuous-Stirred Tank Reactors (CSTRs)
 5.3.1: A Single CSTR
 5.3.2: CSTRs in Series
 5.4: Tubular Reactors
 5.5: Pressure Drop in Reactors
 5.5.1: Pressure Drop and the Rate Law
 5.5.2: Flow Through a Packed Bed
 5.5.3: Pressure Drop in Pipes
 5.5.4: Analytical Solution for Reaction with Pressure Drop
 5.5.5: Robert the Worrier Wonders: What Ifâ#x80
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 5.6: Synthesizing the Design of a Chemical Plant
 Chapter 6: Isothermal Reactor Design: Moles and Molar Flow Rates
 6.1: The Molar Flow Rate Balance Algorithm. 6.2: Mole Balances on CSTRs, PFRs, PBRs, and Batch Reactors6.2.1: Liquid Phase
 6.2.2: Gas Phase
 6.3: Application of the PFR Molar Flow Rate Algorithm to a Microreactor
 6.4: Membrane Reactors
 6.5: Unsteady-State Operation of Stirred Reactors
 6.6: Semibatch Reactors
 6.6.1: Motivation for Using a Semibatch Reactor
 6.6.2: Semibatch Reactor Mole Balances
 Chapter 7: Collection and Analysis of Rate Data
 7.1: The Algorithm for Data Analysis
 7.2: Determining the Reaction Order for Each of Two Reactants Using the Method of Excess
 7.3: Integral Method
 7.4: Differential Method of Analysis.