FREE SHIPPING BOTH WAYS
ON EVERY ORDER!
LIST PRICE:
$207.35

OUR PRICE:
$112.90

You may extend rentals at any time.


Chemical Reactor Analysis and Design, 3rd Edition

ISBN: 9780470565414 | 0470565411
Edition: 3rd
Format: Hardcover
Publisher: Wiley
Pub. Date: 8/1/2010

Why Rent from Knetbooks?

Because Knetbooks knows college students. Our rental program is designed to save you time and money. Whether you need a textbook for a semester, quarter or even a summer session, we have an option for you. Simply select a rental period, enter your information and your book will be on its way!

Top 5 reasons to order all your textbooks from Knetbooks:

  • We have the lowest prices on thousands of popular textbooks
  • Free shipping both ways on ALL orders
  • Most orders ship within 48 hours
  • Need your book longer than expected? Extending your rental is simple
  • Our customer support team is always here to help
SummaryTable of Contents
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, emphasizing 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.
Elements of Reaction Kinetics
Definitions of Chemical Rates
Rate Equations
Coupled Reactions
Reducing the Size of Kinetic Models
Bio-Kinetics
Complex Reactions
Modeling the Rate Coefficient
Kinetics of Heterogeneous Catalytic Reactions
Introduction
Adsorption on Solid Cataly... MORE
Rate Equations
Complex Catalytic Reactions
Experimental Reactors
Model Discrimination and Parameter Estimation
Sequential Design of Experiments
Expert Systems in Kinetics Studies
Transport Processes with Reactions Catalyzed by Solids
Interfacial Gradient Effects
Reaction of a component of a fluid at the surface of a solid
Mass and heat transfer resistances
Concentration or partial pressure and temperature differences
Intraparticle Gradient Effects
Molecular-, Knudsen-, and surface diffusion in pores
Diffusion in a catalyst particle
Diffusion and reaction in a catalyst particle. A continuum model
Falsification of rate coefficient and activation energy by diffusion limitations
Influence of diffusion limitations on the selectivities of coupled reactions
Criteria for the importance of intraparticle diffusion limitations
Multiplicity of steady states in catalyst particles
Combination of external and internal diffusion limitations
Diagnostic experimental criteria for the absence of internal and external mass transfer limitations
Nonisothermal particles
Noncatalytic Gas-Solid Reactions
A Qualitative Discussion of Gas-Solid Reactions
General Model with Interfacial and Intraparticle Gradients
Heterogeneous Model with Shrinking Unreacted Core
Models Accounting Explicitly for the Structure of the Solid
On the Use of More Complex Kinetic Equations
Catalyst Deactivation
Types of Catalyst Deactivation
Kinetics of Catalyst Poisoning
Kinetics of Catalyst Deactivation by Coke Formation
Gas-Liquid Reactions
Introduction
Models for Transfer at a Gas-Liquid Interface
Two-Film Theory
Surface Renewal Theory
Experimental Determination of the Kinetics of Gas-Liquid Reactions
The Modeling of Chemical Reactors
Approach
Aspects of Mass-, Heat- and Momentum Balances
The Fundamental Model Equations
The Batch and Semibatch Reactors
Introduction
The Isothermal Batch Reactor
The Nonisothermal Batch Reactor
Semibatch Reactor Modeling
Optimal Operation Policies and Control Strategies
The Plug Flow Reactor
The Continuity, Energy, and Momentum Equations
Kinetic Studies Using a Tubular Reactor with Plug Flow
Design and Simulation of Tubular Reactors with Plug Flow
The Perfectly Mixed Flow Reactor
Introduction
Mass and Energy Balances
Design for Optimum Selectivity in Simultaneous Reactions
Stability of Operation and Transient Behavior
Fixed Bed Catalytic Reactors
Introduction
The Importance and Scale of Fixed Bed Catalytic Processes
Factors of Progress: Technological Innovations and Increased Fundamental Insight
Factors Involved in the Preliminary Design of Fixed Bed Reactors
Modeling of Fixed Bed Reactors
Pseudohomogeneous Models
The Basic One-Dimensional Model
One-Dimensional Model with Axial Mixing
Two-Dimensional Pseudohomogeneous Models
Heteorgeneous Models
One-Dimensional Model Accounting for Interfacial Gradients
One-Dimensional Model Accounting for Interfacial and Intraparticle Gradients
Two-Dimensional Heterogeneous Models
Complex Flow Patterns
Introduction
Macro- and Micro-Mixing in Reactors
Models Explicitly Accounting for Mixing
Micro- Probability Density Function Methods
Micro-PDF Moment Methods: Computational Fluid Dynamics
Macro-PDF / Residence Time Distribution Methods
Semi-Empirical Models for Reactors with Complex Flow Patterns
Fluidized Bed and Transport Reactors
Introduction
Technological Aspects of Fluidized Bed and Riser Reactors
Some Features of the Fluidization and Transport of Solids
Heat Transfert in Fluidized Beds
Modeling of Fluidized Bed Reactors
Modeling of a Transport of Riser Reactor
Fluidized Bed Reactor Models Considering Detailed Flow Patterns
Catalytic Cracking of Vacuum Gas Oil
Multiphase Flow Reactors
Types of Multiphase Flow Reactors
Design Models for Multiphase Flow Reactors
Specific Design Aspects
Table of Contents provided by Publisher. All Rights Reserved.


Please wait while this item is added to your cart...