Beschreibung
InhaltsangabeChapter1: Introduction PART 1: STEADY-STATE DESIGN OF IDEAL QUATERNARY SYSTEM Chapter 2: Parameter Effects Chapter 3: Economic Comparison of Reactive Distillation with a Conventional Process Chapter 4: Neat Operation versus Using Excess Reactant PART 2: STEADY-STATE DESIGN OF OTHER IDEAL SYSTEMS Chapter 5: Ternary Reactive Distillation Systems Chapter 6: Ternary Decomposition Reaction PART 3: STEADY-STATE DESIGN OF REAL CHEMICAL SYSTEMS Chapter 7: Steady-State Design for Acetic Acid Esterification Chapter 8: Design of TAME Reactive Distillation Systems Chapter 9: Design of MTBE and ETBE Reactive Distillation Columns PART 4: CONTROL OF IDEAL SYSTEMS Chapter 10: Control of Quaternary Reactive Distillation Columns Chapter 11: Control of Excess-Reactant System Chapter 12: Control of Ternary Reactive Distillation Columns PART 5: CONTROL OF REAL SYSTEMS Chapter 13: Control of MeAc/ EtAc/IPAc/BuAc/AmAc Systems Chapter 14: Control of TAME Plantwide Process Chapter 15 Control of MTBE and ETBE Reactive Distillation Columns PART 6: HYBRID AND NON-CONVENTIONAL SYSTEMS Chapter 16: Design and Control of Column/Side- Reactor Systems Chapter 17: Effect of Boiling Point Rankings on the Design of Reactive Distillation Chapter 18: Effects of Feed Tray Locations on the Design and Control of Reactive Distillation APPENDIX A1. Reference A2. Catalog of Types of Real Reactive Distillation Systems
Inhaltsverzeichnis
Chapter1: Introduction PART 1: STEADY-STATE DESIGN OF IDEAL QUATERNARY SYSTEM Chapter 2: Parameter Effects Chapter 3: Economic Comparison of Reactive Distillation with a Conventional Process Chapter 4: Neat Operation versus Using Excess Reactant PART 2: STEADY-STATE DESIGN OF OTHER IDEAL SYSTEMS Chapter 5: Ternary Reactive Distillation Systems Chapter 6: Ternary Decomposition Reaction PART 3: STEADY-STATE DESIGN OF REAL CHEMICAL SYSTEMS Chapter 7: Steady-State Design for Acetic Acid Esterification Chapter 8: Design of TAME Reactive Distillation Systems Chapter 9: Design of MTBE and ETBE Reactive Distillation Columns PART 4: CONTROL OF IDEAL SYSTEMS Chapter 10: Control of Quaternary Reactive Distillation Columns Chapter 11: Control of Excess-Reactant System Chapter 12: Control of Ternary Reactive Distillation Columns PART 5: CONTROL OF REAL SYSTEMS Chapter 13: Control of MeAc/ EtAc/IPAc/BuAc/AmAc Systems Chapter 14: Control of TAME Plantwide Process Chapter 15 Control of MTBE and ETBE Reactive Distillation Columns PART 6: HYBRID AND NON-CONVENTIONAL SYSTEMS Chapter 16: Design and Control of Column/Side- Reactor Systems Chapter 17: Effect of Boiling Point Rankings on the Design of Reactive Distillation Chapter 18: Effects of Feed Tray Locations on the Design and Control of Reactive Distillation APPENDIX A1. Reference A2. Catalog of Types of Real Reactive Distillation Systems
Autorenporträt
William L. Luyben, PHD, is Professor of Chemical Engineering at Lehigh University. In addition to forty years of teaching, Dr. Luyben spent nine years as an engineer with Exxon and DuPont. He has written nine books and more than 200 papers. He was the 2004 recipient of the Computing Practice Award from the CAST Division of the AIChE and was elected in 2005 to the Process Automation Hall of Fame. CHENG-CHING YU, PHD, has spent sixteen years as a Professor at National Taiwan University of Science and Technology and four years at National Taiwan University. He has published over 100 technical papers in the areas of plant-wide process control, reactive distillation, control of microelectronic processes, and modeling of fuel cell systems.
