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 | |
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