Reactive Distillation Design and Control

Introduction Steady State Design of Ideal Quaternary System Parameter Effects Economic Comparison of Reactive Distillation with a Conventional Process Neat Operation versus Using Excess Reactant Part 2: Steady-State Design Of Other Ideal Systems Ternary Reactive Distillation Systems Ternary Decomposition Reaction Part 3: Steady State Design of Real Chemical Systems Steady State Design for Acetic Acid Esterification Design of TAME Reactive Distillation Systems Design of MTBE and ETBE Reactive Distillation Columns Part 4: Control Of Ideal Systems Control of Quaternary Reactive Distillation Columns Control of Excess Reactant System Control of Ternary Reactive Distillation Column Part 5: Control of Real Systems Control of MeAc/ EtAc/IPAc/BuAc/AmAc Systems Control of TAME Plantwide Process Control of MTBE and ETBE Reactive Distillation Columns Part 6: Hybrid And Non-Conventional Systems Design and Control of Column/Side- Reactor Systems Effect of Boiling Point Rankings on the Design of Reactive Distillation Effects of Feed Tray Locations on the Design and Control of Reactive Distillation