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Chemical Engineering Process Simulation [Pehme köide]

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, (University of Nottingham, Malaysia Campus), Edited by , , (Owner and Principal Consultant of specialist consulting company East One-Zero-One Sdn Bhd (), , , , (Department of Chemical and Environmental Engineering, University of Nottingham Malaysia campus)
  • Formaat: Paperback / softback, 464 pages, kõrgus x laius: 229x152 mm, kaal: 790 g
  • Ilmumisaeg: 16-Jul-2017
  • Kirjastus: Elsevier Science Publishing Co Inc
  • ISBN-10: 0128037822
  • ISBN-13: 9780128037829
Teised raamatud teemal:
Chemical Engineering Process SimulationSuurem pilt
  • Formaat: Paperback / softback, 464 pages, kõrgus x laius: 229x152 mm, kaal: 790 g
  • Ilmumisaeg: 16-Jul-2017
  • Kirjastus: Elsevier Science Publishing Co Inc
  • ISBN-10: 0128037822
  • ISBN-13: 9780128037829
Teised raamatud teemal:
Püsilink: https://www.kriso.ee/db/9780128037829.html
Märksõnad:

Chemical Engineering Process Simulation is ideal for students, early career researchers and practitioners, as it guides you through chemical processes and unit operations using the main simulation softwares that are used in the industrial sector. This book will help you to predict the characteristics of a process using mathematical models and computer-aided process simulation tools, plus model and simulate process performance before detailed process design takes place.

Content coverage includes steady and dynamic simulations, the similarities and differences between process simulators, an introduction to operating units and convergence tips and tricks. You will also learn about the use of simulation for risk studies to enhance process resilience, fault finding in abnormal situations and for training operators to control the process in difficult situations. This experienced author team combines industry knowledge with effective teaching methods to make an accessible and clear comprehensive guide to process simulation.

  • Covers the fundamentals of process simulation, theory and advanced applications
  • Includes case studies of various difficulty levels to practice and apply the developed skills
  • Step by step guides to using Aspen Plus and HYSYS for process simulations available on companion site

Muu info

Covers the fundamentals, theory, and advanced applications of chemical engineering process simulation, including use of Aspen Plus and HYSYS
List of Contributors
xv
How to Use This Book xvii
Part 1 Basics of Process Simulation
1 Introduction to Process Simulation
Dominic C.Y. Foo
Rafil Elyas
1.1 Process Design and Simulation
3(2)
1.2 Historical Perspective for Process Simulation
5(1)
1.3 Basic Architectures for Commercial Software
6(2)
1.4 Basic Algorithms for Process Simulation
8(2)
1.4.1 Sequential Modular Approach
8(2)
1.4.2 Equation-Oriented Approach
10(1)
1.5 Incorporation of Process Synthesis Model and Sequential Modular Approach
10(4)
1.6 Ten Good Habits for Process Simulation
14(9)
References
20(3)
2 Registration of New Components
Denny K.S. Ng
Chien Hwa Chong
Nishanth Chemmangattuvalappil
2.1 Registration of Hypothetical Components
23(3)
2.1.1 Hypothetical Component Registration With Aspen HYSYS
23(1)
2.1.2 Hypothetical Component Registration With PRO/II
24(2)
2.2 Registration of Crude Oil
26(25)
References
49(2)
3 Physical Property Estimation for Process Simulation
Rafil Elyas
3.1 Chemical Engineering Processes
51(2)
3.1.1 Separator
52(1)
3.1.2 Heat Exchanger
52(1)
3.1.3 Compressor
53(1)
3.2 Thermodynamic Processes
53(3)
3.2.1 Characteristic Thermodynamic Relationships
54(1)
3.2.2 Maxwell Relationships
55(1)
3.3 Equations of State
56(4)
3.3.1 The Ideal Gas Law (c.1834)
56(1)
3.3.2 Corrections to the Ideal Gas Law (Cubic Equations of State)
57(3)
3.4 Liquid Volumes
60(2)
3.5 Viscosity and Other Properties
62(1)
3.6 Phase Equilibria
62(6)
3.6.1 Vapor Phase Correction
63(2)
3.6.2 Liquid Phase Corrections
65(2)
3.6.3 Bringing It All Together
67(1)
3.7 Flash Calculations
68(4)
3.7.1 "MESH" Equations
69(1)
3.7.2 Bubble Point Flash
70(1)
3.7.3 Dew Point Flash
70(1)
3.7.4 Two-Phase Pressure---Temperature Flash
71(1)
3.7.5 Other Flash Routines
71(1)
3.8 Phase Diagrams
72(5)
3.8.1 Pressure---Temperature Diagrams of Pure Components and Mixtures
72(4)
3.8.2 Retrograde Behavior
76(1)
3.9 Conclusions
77(4)
Exercises
77(2)
References
79(1)
Further Reading
79(2)
4 Simulation of Recycle Streams
Dominic C.Y. Foo
Siewhui Chong
Nishanth Chemmangattuvalappil
4.1 Types of Recycle Streams
81(1)
4.2 Tips in Handling Recycle Streams
82(4)
4.2.1 Analyze the Flowsheet
82(1)
4.2.2 Provide Estimates for Recycle Streams
83(1)
4.2.3 Simplify the Flowsheet
84(1)
4.2.4 Avoid Overspecifying Mass Balance
85(1)
4.2.5 Check for Trapped Material
86(1)
4.2.6 Increase Number of Iterations
86(1)
4.3 Recycle Convergence and Acceleration Techniques
86(11)
Exercises
93(1)
References
93(4)
Part 2 UniSim Design
5 Basics of Process Simulation With UniSim Design
Dominic C.Y. Foo
5.1 Example on n-Octane Production
97(1)
5.2 Stage 1: Basic Simulation Setup
98(3)
5.3 Stage 2: Modeling of Reactor
101(5)
5.4 Stage 3: Modeling of Separation Unit
106(2)
5.5 Stage 4: Modeling of Recycle System
108(6)
5.5.1 Material Recycle System
108(2)
5.5.2 Energy Recycle System
110(4)
5.6 Conclusions
114(5)
Exercises
114(3)
References
117(2)
6 Modeling of a Dew Point Control Unit With UniSim Design
Rafil Elyas
Zhi Hong Li
6.1 Introduction
119(1)
6.2 Preliminary Analysis
120(1)
6.3 Conceptual Design for Dew Point Control Unit
121(3)
6.4 Conceptual Design of Propane Refrigeration System
124(6)
6.4.1 Basic Understanding of a Refrigeration Cycle
125(1)
6.4.2 Degrees of Freedom Analysis
126(1)
6.4.3 Design of Refrigeration Cycle Using a Mollier Diagram
126(3)
6.4.4 Design of Refrigeration System With UniSim Design
129(1)
6.5 Conclusions
130(9)
Exercises
131(1)
Exercise 1 Dew Point Control Unit: Base Model Setup
131(1)
Exercise 2 Dew Point Control Unit: Calculate the Dew Point of the Sales Gas
132(1)
Exercise 3 Dew Point Control Unit: Determining the Chiller Temperature
133(2)
Exercise 4 Propane Refrigeration
135(1)
Reference
135(4)
Part 3 PRO/II
7 Basics of Process Simulation With SimSci PRO/II
Chien Hwa Chong
7.1 Example on n-Octane Production
139(1)
7.2 Stage 1: Basic Simulation Setup
139(2)
7.2.1 Units
139(1)
7.2.2 Component Selection
139(1)
7.2.3 Thermodynamics Method
140(1)
7.3 Stage 2: Modeling of Reactor
141(1)
7.4 Stage 3: Modeling of Separation Units
142(6)
7.5 Stage 4: Modeling of Recycle Systems
148(5)
7.6 Conclusion
153(4)
Exercises
153(2)
References
155(2)
8 Modeling for Biomaterial Drying, Extraction, and Purification Technologies
Chien Hwa Chong
Joanne W.R. Chan
8.1 Introduction
157(1)
8.2 Basic Simulation Setup
158(4)
8.2.1 User-Defined and Solid Components
158(1)
8.2.2 Specification for Process Feed Stream
159(1)
8.2.3 Thermodynamic Data
160(2)
8.3 Modeling of Drying Technology
162(2)
8.4 Modeling of a Conventional Solvent Extractor
164(6)
8.5 Conclusions
170(7)
Acknowledgment
170(1)
Exercise
170(1)
References
171(1)
Appendix A
172(5)
Part 4 ProMax
9 Basics of Process Simulation With ProMax
Rene D. Elms
9.1 Introduction
177(1)
9.2 Setting the Environment
177(3)
9.3 Creating and Adding the Reaction Set
180(2)
9.3.1 Creating the Reaction Set
180(2)
9.3.2 Adding the Reaction Set to the Environment
182(1)
9.4 Flowsheeting and Specification of Blocks and Streams
182(23)
9.4.1 Adding and Connecting the Reactor, Distillation Column, and Splitter Blocks
184(4)
9.4.2 Specifying and Executing the Reactor Inlet, Reactor, Distillation Column, and Splitter Blocks
188(10)
9.4.3 Recycle Loop and Inlet Preheating: Adding and Connecting the Compressor, Cross Exchanger, Heater, Recycle, and Mixer Blocks
198(2)
9.4.4 Specification and Execution of the Compressor, Cross Exchanger, Preheater, Recycle, and Mixer Blocks
200(5)
9.5 Determination of a Recycle Block Guess and Closing of the Recycle Loop
205(1)
9.5.1 Recycle and Mixer Blocks
205(1)
9.5.2 Closing the Recycle Loop
206(1)
9.6 Viewing Results
206(3)
9.7 Conclusion
209(2)
Exercises
209(1)
References
209(2)
10 Modeling of Sour Gas Sweetening With MDEA
Rene D. Elms
10.1 Introduction
211(1)
10.1.1 Background---MDEA Sweetening Example
212(1)
10.2 Process Simulation
212(1)
10.3 Setting the Environment
213(1)
10.4 Adding Blocks to the Flowsheet
214(1)
10.4.1 Adding Stages to the Columns
214(1)
10.4.2 Showing Stages in the Stripper Column Block
215(1)
10.5 Addition and Connection of Process and Energy Streams
215(2)
10.6 Specification of Blocks and Streams
217(9)
10.6.1 Dry Basis Sour Gas Process Stream and the Saturator Block
217(1)
10.6.2 Amine Absorber
218(2)
10.6.3 Rich Flash and the Lean/Rich Exchanger
220(1)
10.6.4 Amine Stripper
221(2)
10.6.5 Recycle Block
223(1)
10.6.6 Makeup/Blowdown Block
224(1)
10.6.7 Circulation Pump and Trim Cooler
225(1)
10.7 Viewing Results
226(7)
References
229(1)
Exercise
229(4)
Part 5 aspenONE Engineering
11 Basics of Process Simulation With Aspen HYSYS
Nishanth Chemmangattuvalappil
Siewhui Chong
11.1 Example on n-Octane Production
233(20)
References
252(1)
Further Reading
252(1)
12 Process Simulation for VCM Production
Siewhui Chong
12.1 Introduction
253(1)
12.2 Process Simulation
253(19)
12.2.1 The Balanced Process
253(19)
12.3 Conclusion
272(3)
Exercises
273(1)
References
273(2)
13 Process Simulation and Design of Acrylic Acid Production
I-Lung Chien
Bor-Yih Yu
Hao-Yeh Lee
13.1 Introduction
275(1)
13.2 Process Overview
275(14)
13.2.1 Reaction Kinetics
276(1)
13.2.2 Phase Equilibrium
277(1)
13.2.3 Upstream Process Flowsheet
277(4)
13.2.4 Downstream Further Separation Flowsheet
281(6)
13.2.5 Sequenced-Separation Process
287(2)
13.3 Effect of Important Design Variables and Examples of Optimization Works
289(9)
13.3.1 Reactor Temperature and Its Size
289(1)
13.3.2 Water Rate Into Absorber
290(1)
13.3.3 Design Variables in Further Separation Section
291(5)
13.3.4 Comparison Between Hybrid Extraction-Distillation Process and Sequenced-Separation Process
296(2)
13.4 Further Comments on Aspen Plus Simulation
298(2)
13.4.1 Reaction Section
298(1)
13.4.2 Further Separation Section
299(1)
13.5 Conclusions
300(5)
Exercises
300(1)
Exercise 1 Furfuryl Alcohol Production Process
300(3)
Exercise 2 2-Methylfuran and Furfuryl Alcohol Coproduction Process
303(2)
Appendix A Cost Equations of Two Exercises
305(130)
A1 Reactor and Column Shell Cost
307(1)
A2 Heat Exchanger Cost
307(1)
A3 Cooling Water Cost
308(1)
A4 Flash Cost
308(1)
A5 Compressor Cost
308(1)
A6 Pump Cost
308(1)
A7 Furnace Cost
308(1)
A8 Column Tray and Tower Internals Cost
309(2)
References
309(2)
14 Design and Simulation of Reactive Distillation Processes
Hao-Yeh Lee
Tyng-Lih Hsiao
14.1 Introduction
311(1)
14.2 Methyl Acetate Reactive Distillation Process
312(10)
14.2.1 Thermodynamic Model
312(2)
14.2.2 Kinetic Model
314(2)
14.2.3 Process Configuration
316(6)
14.3 Butyl Acetate Reactive Distillation Process
322(7)
14.3.1 Thermodynamic Model
322(1)
14.3.2 Reaction Kinetic Model
322(2)
14.3.3 Process Configuration
324(5)
14.4 Isopropyl Acetate Reactive Distillation With Thermally Coupled Configuration
329(14)
14.4.1 Thermodynamic Model
329(3)
14.4.2 Kinetic Model
332(1)
14.4.3 Process Configuration
333(10)
14.5 Conclusion 342 Exercises
343(1)
1 Ethyl Acetate Reactive Distillation Process
343(2)
2 Diphenyl Carbonate Reactive Distillation Process by Using Phenyl Acetate and Diethyl Carbonate as Reactants
345(10)
Appendix: Fortran File Setting for Reactive Distillation
347(5)
References
352(3)
15 Design of Azeotropic Distillation Systems
I-Lung Chien
Bor-Yih Yu
Zi Jie Ai
15.1 Introduction
355(1)
15.2 Azeotropic Separation Without Entrainer
356(3)
15.2.1 Pressure-Swing Distillation
356(2)
15.2.2 Heterogeneous Binary Azeotrope Separation
358(1)
15.2.3 Other Separation Methods
359(1)
15.3 Azeotropic Separation Method by Adding Entrainer
359(5)
15.3.1 Heterogeneous Azeotropic Distillation
359(3)
15.3.2 Extractive Distillation
362(2)
15.3.3 Other Separation Method by Adding Another Component
364(1)
15.4 Aspen Plus Simulations of Two Industrial Examples
364(11)
15.4.1 Methanol and Isopentane Separation
364(5)
15.4.2 Ethanol Dehydration Process
369(6)
15.5 Further Energy Savings via Heat-Integration
375(6)
15.5.1 Feed---Effluent Heat Exchanger
375(1)
15.5.2 Multieffect Distillation Columns
376(2)
15.5.3 Thermally Coupled (Dividing-Wall) Extractive Distillation System
378(1)
15.5.4 Thermally Coupled (Dividing-Wall) Heterogeneous Azeotropic Distillation System
378(3)
15.6 Conclusions
381(6)
Exercises
382(2)
References
384(3)
16 Simulation and Analysis of Heat Exchanger Networks With Aspen Energy Analyzer
Wei-Jyun Wang
Cheng-Liang Chen
16.1 Introduction
387(2)
16.2 Synthesis of Heat Exchanger Networks
389(6)
16.2.1 Basics
389(1)
16.2.2 A Simple One-Hot/One-Cold Heat Recovery Problem
390(3)
16.2.3 A Simple Two-Hot/Two-Cold Heat Recovery Problem
393(2)
16.3 Aspen Energy Analyzer for Analysis and Design of Heat Recovery Systems
395(10)
Exercise
403(1)
References
403(2)
17 Simulation and Analysis of Steam Power Plants With Aspen Utility Planner
Wei-Jyun Wang
Cheng-Liang Chen
17.1 Introduction
405(2)
17.2 Introduction of Aspen Utility Planner
407(2)
17.3 Example---Simulation of a Simple Steam Power Plant
409(26)
17.3.1 Configure Component Properties
410(1)
17.3.2 The Boiler Section
410(6)
17.3.3 The Section of High-Pressure Header, Single-Stage Condensing Turbine, and Single-Stage Condenser
416(3)
17.3.4 The Section of Low-Pressure Header, Steam Letdown, and Steam Desuperheater
419(4)
17.3.5 The Boiler Feed Water Processing Section With Boiler Feed Water Makeup
423(4)
17.3.6 A Single-Stage Back Pressure Turbine and an Electricity System Connected With an External Power Grid and an Electricity Demand
427(2)
17.3.7 Optimization of Steam Utility System Operations
429(4)
Exercise
433(1)
References
434(1)
Index 435
Dr. Nishanth Chemmangattuvalappil is an Associated Professor of Chemical Engineering in the Department of Chemical and Environmental Engineering at University of Nottingham Malaysia. He is also the Head of Sustainable Process Integration Group of the Environmental Research Division of the University of Nottingham, Malaysia campus. He received his PhD in Chemical Engineering from Auburn University in 2010 and worked as a Post-doctoral fellow at the University of Pittsburgh and later at Auburn University. His main areas of expertise include product and molecular design, mixture design and integrated biorefineries. His current work focuses on the application of molecular design concepts on reactive systems, integration of molecular design techniques into the design of biorefineries and carbon capture and storage using ionic liquids. He has co-authored more than 50 peer reviewed international journal articles and two book chapters. In addition, his works have been presented at more than 60 international conferences and at four invited lectures. Owner and Principal Consultant of specialist consulting company East One-Zero-One Sdn Bhd (East101). Dominic Foo is a Professor of Process Design and Integration at the University of Nottingham Malaysia and is the Founding Director for the Centre of Excellence for Green Technologies. He is a Fellow of the Institution of Chemical Engineers (IChemE), Fellow of the Academy of Sciences Malaysia (ASM), Fellow of the Institution of Engineers Malaysia (IEM), Chartered Engineer (CEng) with the Engineering Council UK, Professional Engineer (PEng) with the Board of Engineer Malaysia (BEM), ASEAN Chartered Professional Engineers (ACPE), as well as the President for the Asia Pacific Confederation of Chemical Engineering (APCChE). He is top 1% world-renowned scientist according to Stanford List, working in process integration for resource conservation and CO2 reduction. Professor Foo is an active author, with eight books, more than 190 journal papers and made more than 240 conference presentations, with more than 30 keynote/plenary speeches. Professor Foo is the Editor-in-Chief for Process Integration and Optimization for Sustainability (Springer Nature), Subject Editor for Process Safety & Environmental Protection (Elsevier), and editorial board members for several other renowned journals. He is the winners of the Innovator of the Year Award 2009 of IChemE, Young Engineer Award 2010 of IEM, Outstanding Young Malaysian Award 2012 of Junior Chamber International (JCI), Outstanding Asian Researcher and Engineer 2013 (Society of Chemical Engineers, Japan), and Top Research Scientist Malaysia 2016 (ASM).