Distillation Design and Control Using Aspen Simulation
(Sprache: Englisch)
A timely treatment of distillationcombining steady-state designand dynamic controllabilityAs the world continues to seek new sources of energy, the distillation process remains one of the most important separation methods in the chemical, petroleum, and...
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A timely treatment of distillationcombining steady-state designand dynamic controllability
As the world continues to seek new sources of energy, the distillation process remains one of the most important separation methods in the chemical, petroleum, and energy industries. And as new renewable sources of energy and chemical feedstocks become more universally utilized, the issues of distillation design and control will remain vital to a future sustainable lifestyle.
Distillation Design and Control Using Aspen Simulation introduces the current status and future implications of this vital technology from the dual perspectives of steady-state design and dynamics. Where traditional design texts have focused mainly on the steady-state economic aspects of distillation design, William Luyben also addresses such issues as dynamic performance in the face of disturbances.
Utilizing the commercial simulators Aspen Plus and Aspen Dynamics, the text guides future and practicing chemical engineers first in the development of optimal steady-state designs of distillation systems, and then in the development of effective control structures.
Unique features of the text include:
* In-depth coverage of the dynamics of column design to help develop effective control structures for distillation columns
* Development of rigorous simulations of single distillation columns and sequences of columns
* Coverage of design and control of petroleum fractionators
Encompassing nearly four decades of research and practical developments in this dynamic field, the text represents an important reference for both students and experienced engineers faced with distillation problems.
Klappentext zu „Distillation Design and Control Using Aspen Simulation “
A timely treatment of distillationcombining steady-state designand dynamic controllabilityAs the world continues to seek new sources of energy, the distillation process remains one of the most important separation methods in the chemical, petroleum, and energy industries. And as new renewable sources of energy and chemical feedstocks become more universally utilized, the issues of distillation design and control will remain vital to a future sustainable lifestyle.
Distillation Design and Control Using Aspen Simulation introduces the current status and future implications of this vital technology from the dual perspectives of steady-state design and dynamics. Where traditional design texts have focused mainly on the steady-state economic aspects of distillation design, William Luyben also addresses such issues as dynamic performance in the face of disturbances.
Utilizing the commercial simulators Aspen Plus and Aspen Dynamics, the text guides future and practicing chemical engineers first in the development of optimal steady-state designs of distillation systems, and then in the development of effective control structures.
Unique features of the text include:
In-depth coverage of the dynamics of column design to help develop effective control structures for distillation columns
Development of rigorous simulations of single distillation columns and sequences of columns
Coverage of design and control of petroleum fractionators
Encompassing nearly four decades of research and practical developments in this dynamic field, the text represents an important reference for both students and experienced engineers faced with distillation problems.
Inhaltsverzeichnis zu „Distillation Design and Control Using Aspen Simulation “
- PrefaceChapter 1. Fundamentals of VLE
1.1 Vapor pressure
1.2 Binary VLE phase diagrams
1.3 Physical property methods
1.4 Relative volatility
1.5 Bubblepoint calculations
1.6 Ternary diagrams
1.7 VLE non-ideality
1.8 Residue curves for ternary systems
1.9 Conclusion
Chapter 2. Analysis of Distillation Columns
2.1 Design degrees of freedom
2.2 Binary McCabe-Thiele method
2.3 Approximate multi-component methods
2.4 Analysis of ternary systems using DISTIL
2.5 Conclusion
Chapter 3. Setting Up a Steady-State Simulation
3.1 Configuring a new simulation
3.2 Specifying chemical components and physical properties
3.3 Specifying stream properties
3.4 Specifying parameters of equipment
3.5 Running the simulation
3.6 Using design spec/vary function
3.7 Finding the optimum feed tray and minimum conditions
3.8 Column sizing
3.9 Conclusion
Chapter 4. Distillation Economic Optimization
4.1 Heuristic optimization
4.2 Economic basis
4.3 Results
4.4 Operating optimization
4.5 Conclusion
Chapter 5. More Complex Distillation Systems
5.1 Methyl actate/methanol/water system
5.2 Ethanol dehydration
5.3 Heat-integrated columns
5.4 Conclusion
Chapter 6. Steady-State Calculations for Control Structure Selection
6.1 Summary of methods
6.2 Binary propane/isobutane system
6.3 Ternary BTX system
6.4 Multi-component hydrocarbon system
6.5 Ternary azeotropic system
6.6 Conclusion
Chapter 7. Converting from Steady State to Dynamic Simulation
7.1 Equipment sizing
7.2 Exporting to Aspen Dynamics
7.3 Opening the dynamic simulation in Aspen Dynamics
7.4 Installing basic controllers
7.5 Installing temperature and composition controllers
7.6 Performance evaluation
7.7 Comparison with economic optimum design
7.8 Conclusion
Chapter 8. Control of More Complex Columns
8.1 Methyl acetate column
8.2 Columns with partial condensers
8.3 Control of heat-integrated distillation columns
8.4 Control of azeotropic columns/decanter system
8.5
... mehr
Conclusion
Chapter 9. Reactive Distillation
9.1 Introduction
9.2 Types of reactive distillation systems
9.3 TAME process basics
9.4 TAME reaction kinetics and VLE
9.5 Plantwide control structure
9.6 Conclusion
Chapter 10. Control of Sidestream Columns
10.1 Liquid sidestream column
10.2 Vapor sidestream column
10.3 Liquid sidestream column with stripper
10.4 Vapor sidestream column with rectifier
10.5 Sidestream purge column
10.6 Conclusion
Chapter 11. Control of Petroleum Fractionators
11.1 Petroleum fractions
11.2 Characterization of crude oil
11.3 Steady-state design of preflash column
11.4 Control of preflash column
11.5 Steady-state design of pipestill
11.6 Control of pipestill
11.7 Conclusion
Chapter 9. Reactive Distillation
9.1 Introduction
9.2 Types of reactive distillation systems
9.3 TAME process basics
9.4 TAME reaction kinetics and VLE
9.5 Plantwide control structure
9.6 Conclusion
Chapter 10. Control of Sidestream Columns
10.1 Liquid sidestream column
10.2 Vapor sidestream column
10.3 Liquid sidestream column with stripper
10.4 Vapor sidestream column with rectifier
10.5 Sidestream purge column
10.6 Conclusion
Chapter 11. Control of Petroleum Fractionators
11.1 Petroleum fractions
11.2 Characterization of crude oil
11.3 Steady-state design of preflash column
11.4 Control of preflash column
11.5 Steady-state design of pipestill
11.6 Control of pipestill
11.7 Conclusion
... weniger
Autoren-Porträt von William L. Luyben
WILLIAM L. LUYBEN, PhD, is Professor of Chemical Engineering at Lehigh University. In addition to thirty-eight years of teaching, Dr. Luyben spent nine years as an engineer with Exxon and DuPont. Over the years, he has written eight 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.
Bibliographische Angaben
- Autor: William L. Luyben
- 2006, 1. Auflage, 360 Seiten, Maße: 18,9 x 23,7 cm, Gebunden, Englisch
- Verlag: Wiley & Sons
- ISBN-10: 0471778885
- ISBN-13: 9780471778882
Sprache:
Englisch
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