E-Book, Englisch, 472 Seiten, E-Book
Luyben / Chien Design and Control of Distillation Systems for Separating Azeotropes
1. Auflage 2011
ISBN: 978-1-118-20983-7
Verlag: John Wiley & Sons
Format: EPUB
Kopierschutz: 0 - No protection
E-Book, Englisch, 472 Seiten, E-Book
ISBN: 978-1-118-20983-7
Verlag: John Wiley & Sons
Format: EPUB
Kopierschutz: 0 - No protection
Hands-on guidance for the design, control, and operation ofazeotropic distillation systems
Following this book's step-by-step guidance, readers learn tomaster tested and proven methods to overcome a major problem inchemical processing: the distillation and separation of azeotropes.Practical in focus, the book fully details the design, control, andoperation of azeotropic distillation systems, using rigoroussteady-state and dynamic simulation tools.
Design and Control of Distillation Systems for SeparatingAzeotropes is divided into five parts:
* Fundamentals and tools
* Separations without adding other components
* Separations using light entrainer (heterogeneous azeotropicdistillation)
* Separations using heavy entrainer (extractive distillation)
* Other ways for separating azeotropes
The distillation methods presented cover a variety of importantindustrial chemical systems, including the processing of biofuels.For most of these chemical systems, the authors explain how toachieve economically optimum steady-state designs. Moreover,readers learn how to implement practical control structures thatprovide effective load rejection to manage disturbances inthroughput and feed composition.
Trade-offs between steady-state energy savings and dynamiccontrollability are discussed, helping readers design and implementthe distillation system that best meets their particular needs. Inaddition, economic and dynamic comparisons between alternativemethods are presented, including an example of azeotropicdistillation versus extractive distillation for theisopropanol/water system.
With its focus on practical solutions, Design and Control ofDistillation Systems for Separating Azeotropes is ideal forengineers facing a broad range of azeotropic separation problems.Moreover, this book is recommended as a supplemental text forundergraduate and graduate engineering courses in design, control,mass transfer, and bio-processing.
Autoren/Hrsg.
Weitere Infos & Material
PREFACE.
ACKNOWLEDGEMENTS.
PART 1 FUNDAMENTALS AND TOOLS.
1 INTRODUCTION.
1.1 History.
1.2 Applications.
1.3 Literature.
1.4 Multiple Steady States.
References.
2 PHASE EQUILIBRIUM.
2.1 Phase Equilibrium Relationships.
2.2 Equations Describing Phase Equilibrium Relationships.
2.3 Diagrams For Binary Systems.
2.4 Ternary Diagrams.
2.5 Data Regression.
2.6 Group Contribution Method.
2.7 Conclusion.
References.
3 STEADY-STATE DESIGN IN ASPEN PLUS.
3.1 Building a Steady-State Model.
3.2 Unit Operation Blocks Used in this Book.
3.3 Add a Nondatabank Component.
3.4 Conclusion.
References.
4 DYNAMICS AND CONTROL IN ASPEN DYNAMICS.
4.1 Sizing of Process Vessels.
4.2 Sizing of Pumps, Compressors, and Control Valves.
4.3 Controllers and Dynamic Elements.
4.4 Controller Tuning.
4.5 Ratio and Cascade Control.
4.6 Conclusion.
PART 2 SEPARATIONS WITHOUT ADDING OTHER COMPONENTS.
5 PRESSURE-SWING AZEOTROPIC DISTILLATION.
5.1 Tetrahydrofuran-Water System.
5.2 Acetone-Methanol System.
5.3 Pentane-Methanol System.
5.4 Conclusion.
References.
6 PRESSURE SWING WITH HEAT INTEGRATION.
6.1 THF-Water System Steady-State Design with Heat Integration.
6.2 THF-Water System Dynamics and Control.
6.3 Heat Integration in an Acetone-Methanol System.
6.4 Conclusion.
References.
7 HETEROGENEOUS BINARY AZEOTROPES.
7.1 n-Butanol-Water System.
7.2 Phase Equilibrium.
7.3 Steady-State Design.
7.4 Dynamics and Control.
7.5 Conclusion.
References.
PART 3 SEPARATIONS USING A LIGHT ENTRAINER (HETEROGENEOUS AZEOTROPIC DISTILLATION).
8 ISOPROPANOL-WATER (CYCLOHEXANE AS THE ENTRAINER).
8.1 Feasible Column Sequence for the Separation.
8.2 Steady-State Design of an Isopropanol-Water System.
8.3 Overall Control Strategy Development.
8.4 Conclusion.
References.
9 ACETIC ACID-WATER (ISOBUTYL ACETATE AS THE ENTRAINER).
9.1 Comparison of Three Candidate Entrainers.
9.2 Control Strategy Development.
9.3 Industrial Column with Preliminary Dynamic Simulations.
9.4 Industrial Column with Continuous Side-Stream Draw Off.
9.5 Side Draw with a Practical Automatic Purging Strategy.
9.6 Conclusion.
References.
PART 4 SEPARATIONS USING HEAVY ENTRAINER (EXTRACTIVE DISTILLATION).
10 ISOPROPANOL-WATER (DIMETHYL SULFOXIDE AS THE ENTRAINER).
10.1 Comparing Entrainers: Dimethyl Sulfoxide Versus Ethylene Glycol.
10.2 Steady-State Design and Economical Analysis.
10.3 Overall Control Strategy Development.
10.4 Conclusion.
References.
11 EXTRACTIVE DISTILLATION OF THE ACETONE-METHANOL SYSTEM.
11.1 Acetone-Methanol-Water Phase Equilibrium.
11.2 Steady-State Design.
11.3 Dynamics and Control.
11.4 Heat-Integrated System.
11.5 Effect of Solvent on Controllability.
11.6 Conclusion.
References.
12 MAXIMUM-BOILING AZEOTROPES.
12.1 Acetone-Chloroform System Steady-State Design.
12.2 Dynamics and Control.
12.3 Conclusion.
Reference.
PART 5 OTHER WAYS FOR SEPARATING AZEOTROPES.
13 BATCH DISTILLATION OF AZEOTROPES.
13.1 Batch Extractive Distillation (Acetone-Methanol with Water as the Entrainer).
13.2 Batch Extractive Distillation (Isopropanol-Water with DMSO as the Entrainer).
13.3 Acetic Acid Dehydration Via Heteroazeotropic Batch Distillation.
13.4 Multivessel Heteroazeotropic Batch Distillation.
13.5 Conclusion.
References.
14 HYBRID DISTILLATION-PERVAPORATION SYSTEMS.
14.1 Introduction.
14.2 Pervaporation Model.
14.3 Pervaporation-Column System.
14.4 Dynamics and Control.
14.5 Process Modification.
14.6 Conclusion.
References.
INDEX.