Process Analysis and Simulation in Chemical Engineering
(Sprache: Englisch)
This book offers a comprehensive coverage of process simulation and flowsheeting, useful for undergraduate students of Chemical Engineering and Process Engineering as theoretical and practical support in Process Design, Process Simulation, Process...
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Klappentext zu „Process Analysis and Simulation in Chemical Engineering “
This book offers a comprehensive coverage of process simulation and flowsheeting, useful for undergraduate students of Chemical Engineering and Process Engineering as theoretical and practical support in Process Design, Process Simulation, Process Engineering, Plant Design, and Process Control courses. The main concepts related to process simulation and application tools are presented and discussed in the framework of typical problems found in engineering design. The topics presented in the chapters are organized in an inductive way, starting from the more simplistic simulations up to some complex problems.
Inhaltsverzeichnis zu „Process Analysis and Simulation in Chemical Engineering “
- PrefaceChapter 1
Process Simulation in Chemical Engineering
1.1. Introduction
1.2. Chemical process simulators
1.3. Types of process simulators
1.3.1. Simultaneous or Equation oriented simulators
1.3.2. Hybrid simulators
1.3.3. Aspen Plus® and Aspen Hysys®
1.4. Applications of process simulation
1.4.1. Computer-aided design
1.4.2. Process optimization
1.4.3. Solution of operating problems
1.4.4. Other applications
1.5. Convergence Analysis
1.5.1. Convergence Methods (Babu, 2004 ; Dimian, 2003 ; Seider, Seader & Lewin, 2004)
1.5.2. Problems with simple recycles
1.5.3. Partitioning and topological analysis
1.5.4. Nested recycles
1.6. Introductory example
1.6.1. Problem description
1.6.2. Simulation using Aspen HYSYS®
1.6.3. Simulation using Aspen Plus®
1.7. Sensitivity Analysis
1.7.1. Sensitivity Analysis in Aspen Plus®
1.7.2. Sensitivity Analysis in Aspen HYSYS®
1.8. Design specifications
1.9. Summary
1.10. Problems
Chapter 2
Thermodynamic and property models
2.1. Introduction
2.2. Ideal model
2.3. Equations of State
2.4. Activity coefficient models
2.5. Special Models
2.5.1. Polymeric systems
2.5.2. Electrolytic System
2.6. Integration of the activity models with equations of the state
2.7. Selection of thermodynamic model
2.8. Example of property model selection
2.9. Example of phase diagram
2.10. Example of parameter adjustment
2.11. Hypothetical components
2.11.1. Usage in Aspen HYSYS®
2.11.2. Usage in Aspen Plus®
2.12. Summary
2.13. Problems
Chapter 3
Fluid Handling Equipment
3.1 Introduction
3.2 General Aspects
3.2.1 Background
3.2.2 Piping
3.2.3 Pumps
3.2.4 Compressors and Expanders
3.3 Modules available in Aspen Plus®
3.4 Modules available in Aspen HYSYS®
3.5 Gas Handling Introductory Example
3.5.1 Problem Description
3.5.2 Simulation in Aspen HYSYS®
3.5.3 Results Analysis
3.6 Liquid Handling Introductory Example
3.6.1 Problem Description
3.6.2 Process Simulation
3.6.3 Results Analysis
3.7
... mehr
Summary
3.8 Problems
Chapter 4
Heat Exchange Equipment and Heat Integration
4.1 Introduction
4.2 Types of Programs Available
4.3 General Aspects
4.3.1 Shortcut Calculation (Holman, 1999)
4.3.2 Rigorous Calculation (Holman, 1999)
4.3.3 Calculation models
4.4 Modules available in Aspen Plus®
4.5 Modules available in Aspen HYSYS®
4.5.1 Thermodynamic Heat Exchangers
4.6 Introductory Example
4.6.1 Problem Description
4.6.2 Simulation in Aspen Plus®
4.6.3 Simulation in Aspen HYSYS®
4.6.4 Simulation in Aspen HTFS®
4.6.5 Results Analysis
4.7 Process Heat Integration
4.7.1 Introduction
4.7.2 Theoretical principles
4.7.3 Aspen Energy Analyzer
4.8 Summary
4.9 Problems
Chapter 5
Chemical reactors
5.1 Introduction
5.2 General Aspects
5.3. Equations for Reactor Design
5.4. Modules Available in Aspen Plus®
5.5. Available modules in ASPEN HYSYS®
5.6. Introductory example of Reactors
5.6.1. Problem Description
5.6.2. Simulation in Aspen Hysys®
5.6.3. Results Analysis
5.7. Propylene Glycol Reactor Example
5.7.1. General Aspects
5.7.2. Process Simulation in Aspen Plus®
5.7.3. Results Analysis
5.8. Methanol Reforming Reactor
5.8.1. Problem Description
5.8.2. Simulation in Aspen Plus®
5.8.3. Simulation in Aspen Hysys®
5.8.4. Analysis And Results Comparison
5.9. Summary
5.10. Problems
Chapter 6
Gas-Liquid Separation Operations
6.1 Introduction
6.2 Available modules in Aspen Plus®
6.2.1 Shortcut Methods
6.2.2 Rigorous Methods
6.3 Modules available in Aspen Hysys®
6.3.1 Predefined Columns
6.3.2 Shortcut Calculation Model
6.3.3 Column Interface
6.4 Distillation Introductory Example
6.4.1 Problem Description
6.4.2 Simulation In Aspen Plus®
6.4.3 Simulation in Aspen Hysys®
6.4.4 Results Analysis and Comparison
6.5 Absorption Introductory Example
6.5.1 Problem Description
6.5.2 Process Simulation
6.6 Enhanced Distillation
6.6.1 Residue Curves Map (RCM)
6.6.2 Extractive Distillation
6.7 Non-Equilibrium Models
6.7.1 Non-Equilibrium Model Example
6.8 Columns Thermal And Hydraulic Analysis
6.8.1 Application Exercise
6.9 Summary
6.10 Problems
Chapter 7
Process Optimization in Chemical Engineering
7.1. Introduction
7.2 Formulation of optimization problem
7.2.1. Degrees of Freedom
7.2.2. Objective Function
7.2.3. Classification of optimization problems
7.3. Optimization in Sequential Simulators
7.4. Introductory Example
7.4.1. Aspen Plus® Simulation
7.4.2. Sensitivity Analysis
7.4.3. Results
7.5. Summary
7.6. Problems
Chapter 8
Dynamic Process Analysis
8.1. Introduction
8.2. General Aspects
8.2.1. Process control
8.2.2. Controllers
8.3. Introductory example
8.4. Gasoline blending
8.5. Pressure Relief Valves
8.5.1. General Aspects
8.5.2. Application example
8.6. Control of the propylene glycol reactor
8.7. Control of distillation columns
8.7.1. General aspects
8.7.2. Distillation column example
8.8. Summary
8.9. Problems
Chapter 9
Solids Operations in Process Simulators
9.1 Introduction
9.2 General Aspects
9.2.1 Separation or classification
9.2.2 Comminution
9.2.3 Filtration
9.2.4 Crystallization
9.2.5 Particle Size Distribution Meshes (PSD)
9.3 Modules in Aspen Plus®
9.4 Modules in Aspen HYSYS®
9.5 Crusher Introductory Example
9.5.1 General Aspects
9.5.2 Simulation in Aspen Plus®
9.5.3 Results Analysis
9.6 Solids handling example
9.6.1 General Aspects
9.6.2 Simulation in Aspen Plus®
9.6.3 Results Analysis
9.7 Summary
Chapter 10
Case Studies
10.1. Introduction
10.2. Simulation of Nylon 6,6 Resin Reactor
10.2.1. Problem Description
10.2.2. Polymerization reaction kinetics
10.2.3. Continuous Production
10.2.4. Batch Production
10.2.5. Results Comparison
3.8 Problems
Chapter 4
Heat Exchange Equipment and Heat Integration
4.1 Introduction
4.2 Types of Programs Available
4.3 General Aspects
4.3.1 Shortcut Calculation (Holman, 1999)
4.3.2 Rigorous Calculation (Holman, 1999)
4.3.3 Calculation models
4.4 Modules available in Aspen Plus®
4.5 Modules available in Aspen HYSYS®
4.5.1 Thermodynamic Heat Exchangers
4.6 Introductory Example
4.6.1 Problem Description
4.6.2 Simulation in Aspen Plus®
4.6.3 Simulation in Aspen HYSYS®
4.6.4 Simulation in Aspen HTFS®
4.6.5 Results Analysis
4.7 Process Heat Integration
4.7.1 Introduction
4.7.2 Theoretical principles
4.7.3 Aspen Energy Analyzer
4.8 Summary
4.9 Problems
Chapter 5
Chemical reactors
5.1 Introduction
5.2 General Aspects
5.3. Equations for Reactor Design
5.4. Modules Available in Aspen Plus®
5.5. Available modules in ASPEN HYSYS®
5.6. Introductory example of Reactors
5.6.1. Problem Description
5.6.2. Simulation in Aspen Hysys®
5.6.3. Results Analysis
5.7. Propylene Glycol Reactor Example
5.7.1. General Aspects
5.7.2. Process Simulation in Aspen Plus®
5.7.3. Results Analysis
5.8. Methanol Reforming Reactor
5.8.1. Problem Description
5.8.2. Simulation in Aspen Plus®
5.8.3. Simulation in Aspen Hysys®
5.8.4. Analysis And Results Comparison
5.9. Summary
5.10. Problems
Chapter 6
Gas-Liquid Separation Operations
6.1 Introduction
6.2 Available modules in Aspen Plus®
6.2.1 Shortcut Methods
6.2.2 Rigorous Methods
6.3 Modules available in Aspen Hysys®
6.3.1 Predefined Columns
6.3.2 Shortcut Calculation Model
6.3.3 Column Interface
6.4 Distillation Introductory Example
6.4.1 Problem Description
6.4.2 Simulation In Aspen Plus®
6.4.3 Simulation in Aspen Hysys®
6.4.4 Results Analysis and Comparison
6.5 Absorption Introductory Example
6.5.1 Problem Description
6.5.2 Process Simulation
6.6 Enhanced Distillation
6.6.1 Residue Curves Map (RCM)
6.6.2 Extractive Distillation
6.7 Non-Equilibrium Models
6.7.1 Non-Equilibrium Model Example
6.8 Columns Thermal And Hydraulic Analysis
6.8.1 Application Exercise
6.9 Summary
6.10 Problems
Chapter 7
Process Optimization in Chemical Engineering
7.1. Introduction
7.2 Formulation of optimization problem
7.2.1. Degrees of Freedom
7.2.2. Objective Function
7.2.3. Classification of optimization problems
7.3. Optimization in Sequential Simulators
7.4. Introductory Example
7.4.1. Aspen Plus® Simulation
7.4.2. Sensitivity Analysis
7.4.3. Results
7.5. Summary
7.6. Problems
Chapter 8
Dynamic Process Analysis
8.1. Introduction
8.2. General Aspects
8.2.1. Process control
8.2.2. Controllers
8.3. Introductory example
8.4. Gasoline blending
8.5. Pressure Relief Valves
8.5.1. General Aspects
8.5.2. Application example
8.6. Control of the propylene glycol reactor
8.7. Control of distillation columns
8.7.1. General aspects
8.7.2. Distillation column example
8.8. Summary
8.9. Problems
Chapter 9
Solids Operations in Process Simulators
9.1 Introduction
9.2 General Aspects
9.2.1 Separation or classification
9.2.2 Comminution
9.2.3 Filtration
9.2.4 Crystallization
9.2.5 Particle Size Distribution Meshes (PSD)
9.3 Modules in Aspen Plus®
9.4 Modules in Aspen HYSYS®
9.5 Crusher Introductory Example
9.5.1 General Aspects
9.5.2 Simulation in Aspen Plus®
9.5.3 Results Analysis
9.6 Solids handling example
9.6.1 General Aspects
9.6.2 Simulation in Aspen Plus®
9.6.3 Results Analysis
9.7 Summary
Chapter 10
Case Studies
10.1. Introduction
10.2. Simulation of Nylon 6,6 Resin Reactor
10.2.1. Problem Description
10.2.2. Polymerization reaction kinetics
10.2.3. Continuous Production
10.2.4. Batch Production
10.2.5. Results Comparison
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Autoren-Porträt von Iván Darío Gil Chaves, Javier Ricardo Guevara López, Gerardo Rodríguez Niño, Alexander Leguizamón Robayo, José Luis García Zapata
Iván Darío Gil Chaves Dr. Gil is a Professor of Chemical Engineering at the Department of Chemical and Environmental Engineering at National University of Colombia - Sede Bogotá. He received B.S. and MSc degrees from National University of Colombia. He obtained his Ph.D. in Chemical Engineering at University of Lorraine (France) and National University of Colombia (under joint supervision). Gil has participated in some industrial projects in the area of process design and control; mainly he has collaborated with representatives of Aspen Technology in Colombia in advanced process control applications. He was also instructor at Andes University in Colombia. Currently, he teaches university courses in modeling and simulation, process control, reaction engineering and process design. In addition, he presents some short courses in advanced process control and process synthesis and optimization. Dr. Gil is co-author of several publications in peer review journals on process design and control. His research interests include biofuels, with emphasis on fuel ethanol and the use of extractive distillation to dehydrate mixtures ethanol-water; modeling, simulation and control of reaction and separation operations; nonlinear geometric control and vapor liquid equilibrium.
Javier Ricardo Guevara López
Javier Guevara holds a B.Sc. in Chemical Engineering from National University of Colombia. He is a process engineer with experience developing Conce
Bibliographische Angaben
- Autoren: Iván Darío Gil Chaves , Javier Ricardo Guevara López , Gerardo Rodríguez Niño , Alexander Leguizamón Robayo , José Luis García Zapata
- 2015, 1st ed. 2016, XVIII, 523 Seiten, 426 farbige Abbildungen, Maße: 16 x 24,1 cm, Gebunden, Englisch
- Verlag: Springer, Berlin
- ISBN-10: 3319148117
- ISBN-13: 9783319148113
- Erscheinungsdatum: 07.12.2015
Sprache:
Englisch
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