rent-now

Rent More, Save More! Use code: ECRENTAL

5% off 1 book, 7% off 2 books, 10% off 3+ books

9780470377796

Reactive Distillation Design and Control

by ;
  • ISBN13:

    9780470377796

  • ISBN10:

    0470377798

  • Format: eBook
  • Copyright: 2009-03-01
  • Publisher: Wiley-AIChE
  • Purchase Benefits
  • Free Shipping Icon Free Shipping On Orders Over $35!
    Your order must be $35 or more to qualify for free economy shipping. Bulk sales, PO's, Marketplace items, eBooks and apparel do not qualify for this offer.
  • eCampus.com Logo Get Rewarded for Ordering Your Textbooks! Enroll Now
List Price: $142.00
We're Sorry.
No Options Available at This Time.

Summary

After an overview of the fundamentals, limitations, and scope of reactive distillation, this book uses rigorous models for steady-state design and dynamic analysis of different types of reactive distillation columns and quantitatively compares the economics of reactive distillation columns with conventional multi-unit processes. It goes beyond traditional steady-state design that primarily considers the capital investment and energy costs when analyzing the control structure and the dynamic robustness of disturbances, and discusses how to maximize the economic and environmental benefits of reactive distillation technology.

Table of Contents

Introduction
History
Basics of Reactive Distillation
Neat Operation versus Excess Reactant
Limitations
Scope
Computational Methods
References
Steady-State Design of Ideal Quaternary System
Parameter Effects
Effect of Holdup on Reactive Trays
Effect of Number of Reactive Trays
Effect of Pressure
Effect of Chemical Equilibrium Constant
Effect of Relative Volatilities
Effect of Number of Stripping and Rectifying Trays
Effect of Reactant Feed Location
Conclusion
Economic Comparison of Reactive Distillation with a Conventional Process
Conventional Multi-Unit Process
Reactive Distillation Design
Results for Different Chemical Equilibrium Constants
Results for Temperature-Dependent Relative Volatilities
Conclusion
Neat Operation versus Using Excess Reactant
Introduction
Neat Reactive Column
Two-Column System with Excess B
Two-Column System with 20% Excess A
Economic Comparison
Conclusion
Steady-State Design of Other Ideal Systems
Ternary Reactive Distillation Systems
Ternary System without Inerts
Ternary System with Inerts
Conclusion
Ternary Decomposition Reaction
Intermediate Boiling Reactant
Heavy Key Reactant with Two Column Configuration
Heavy Key Reactant with One Column Configuration
Conclusion
Steady-State Design of Real Chemical Systems
Steady-State Design for Acetic Acid Esterification
Reaction Kinetics and Phase Equilibrium
Process Flowsheets
Steady-State Design
Process Characteristics
Discussion
Conclusion
Design of TAME Reactive Distillation Systems
Chemical Kinetics and Phase Equilibrium
Component Balances
Effect of Parameters on Reactive Column
Pressure-Swing Methanol Separation Section
Extractive Distillation Methanol Separation Section
Economic Comparison
Conclusion
Design of MTBE and ETBE Reactive Distillation Columns
MTBE Process
ETBE Process
Conclusion
Control of Ideal Systems
Control of Quaternary Reactive Distillation Columns
Introduction
Steady-State Design
Control Structures
Selection of Control Tray Location
Closedloop Performance
Using More Reactive Trays
Increasing Holdup on Reactive Trays
Rangeability
Conclusion
Control of Excess-Reactant System
Control Degrees of Freedom
Single Reactive Column Control Structures
Control of Two-Column System
Conclusion
Control of Ternary Reactive Distillation Columns
Ternary System without Inerts
Ternary System with Inerts
Ternary A?B+C System: Intermediate Boiling Reactant
Ternary A?B+C System: Heavy Reactant with Two-Column Configuration
Ternary A?B+C System: Heavy Reactant with Single Column
Control Of Real Systems
Control of MeAc/ EtAc/IPAc/BuAc/AmAc Systems
Process Characteristic
Control Structure Design
Extension to Composition Control
Conclusion
Control of TAME Plantwide Process
Process Studied
Control Structure
Results
Conclusion
Control of MTBE and ETBE Reactive Distillation Columns
MTBE Control
ETBE Control
Hybrid and Non-Conventional Systems
Design and Control of Column/Side- Reactor Systems
Introduction
Design for Quaternary Ideal System
Control of Quaternary Ideal System
Design of Column/Side-Reactor Process for Ethyl Acetate System
Control of Column/Side-Reactor Process for Ethyl Acetate System
Conclusion
Effect of Boiling Point Rankings on the Design of Reactive Distillation
Process and Classification
Process Configurations
Relaxation and Convergence
Results and Discussion
Conclusion
Effects of Feed Tray Locations on the Design and Control of Reactive Distillation
Process Characteristics
Effects of Relative Volatilities
Effects of Reaction Kinetics
Operation and Control
Conclusion
Appendix
Reference
Catalog of Types of Real Reactive Distillation Systems
Table of Contents provided by Publisher. All Rights Reserved.

Supplemental Materials

What is included with this book?

The New copy of this book will include any supplemental materials advertised. Please check the title of the book to determine if it should include any access cards, study guides, lab manuals, CDs, etc.

The Used, Rental and eBook copies of this book are not guaranteed to include any supplemental materials. Typically, only the book itself is included. This is true even if the title states it includes any access cards, study guides, lab manuals, CDs, etc.

Rewards Program