
Chemical Engineering Design
Principles, Practice and Economics of Plant and Process Design
- 3rd Edition - July 14, 2021
- Imprint: Butterworth-Heinemann
- Authors: Gavin Towler, Ray Sinnott
- Language: English
- Paperback ISBN:9 7 8 - 0 - 1 2 - 8 2 1 1 7 9 - 3
- eBook ISBN:9 7 8 - 0 - 3 2 3 - 8 5 0 4 8 - 3
Chemical Engineering Design: Principles, Practice and Economics of Plant and Process Design is one of the best-known and most widely adopted texts available for students of chemic… Read more

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Request a sales quote- Provides students with a text of unmatched relevance for chemical process and plant design courses and for the final year capstone design course
- Written by practicing design engineers with extensive undergraduate teaching experience
- Contains more than 100 typical industrial design projects drawn from a diverse range of process industries
NEW TO THIS EDITION
- Includes new content covering food, pharmaceutical and biological processes and commonly used unit operations
- Provides updates on plant and equipment costs, regulations and technical standards
- Includes limited online access for students to Cost Engineering’s Cleopatra Enterprise cost estimating software
- Cover image
- Title page
- Table of Contents
- Copyright
- Preface to the Third Edition
- How To Use This Book
- Acknowledgments
- I. Process design
- Chapter 1. Introduction to design
- 1.1. Introduction
- 1.2. Nature of design
- 1.3. The organization of a chemical engineering project
- 1.4. Project documentation
- 1.5. Codes and standards
- 1.6. Design factors (design margins)
- 1.7. Systems of units
- 1.8. Product design
- Chapter 2. Process flowsheet development
- 2.1. Introduction
- 2.2. Flowsheet presentation
- 2.3. The anatomy of a chemical manufacturing process
- 2.4. Selection, modification, and improvement of commercially proven processes
- 2.5. Revamps of existing plants
- 2.6. Synthesis of novel flowsheets
- 2.7. PFD review
- 2.8. Overall procedure for flowsheet development
- Chapter 3. Utilities and energy-efficient design
- 3.1. Introduction
- 3.2. Utilities
- 3.3. Energy recovery
- 3.4. Waste stream combustion
- 3.5. Heat exchanger networks
- 3.6. Energy management in unsteady processes
- Chapter 4. Process simulation
- 4.1. Introduction
- 4.2. Process simulation programs
- 4.3. Specification of components
- 4.4. Selection of physical property models
- 4.5. Simulation of unit operations
- 4.6. User models
- 4.7. Flowsheets with recycle
- 4.8. Flowsheet optimization
- 4.9. Dynamic simulation
- Chapter 5. Instrumentation and process control
- 5.1. Introduction
- 5.2. The P&I diagram
- 5.3. Process instrumentation and control
- 5.4. Conventional control schemes
- 5.5. Alarms, safety trips, and interlocks
- 5.6. Batch process control
- 5.7. Computer control systems
- Chapter 6. Materials of construction
- 6.1. Introduction
- 6.2. Material properties
- 6.3. Mechanical properties
- 6.4. Corrosion resistance
- 6.5. Selection for corrosion resistance
- 6.6. Material costs
- 6.7. Contamination
- 6.8. Commonly used materials of construction
- 6.9. Plastics as materials of construction for chemical plants
- 6.10. Ceramic materials (silicate materials)
- 6.11. Carbon
- 6.12. Protective coatings
- 6.13. Design for corrosion resistance
- Chapter 7. Capital cost estimating
- 7.1. Introduction
- 7.2. Components of capital cost
- 7.3. Accuracy and purpose of capital cost estimates
- 7.4. Order-of-magnitude estimates
- 7.5. Estimating purchased equipment costs
- 7.6. Estimating installed costs: The factorial method
- 7.7. Cost escalation
- 7.8. Location factors
- 7.9. Estimating off-site capital costs
- 7.10. Computer tools for cost estimating
- 7.11. Validity of cost estimates
- Chapter 8. Estimating revenues and production costs
- 8.1. Introduction
- 8.2. Costs, revenues, and profits
- 8.3. Product and raw material prices
- 8.4. Estimating variable production costs
- 8.5. Estimating fixed production costs
- 8.6. Summarizing revenues and production costs
- 8.7. References
- 8.8. Nomenclature
- 8.9. Problems
- Chapter 9. Economic evaluation of projects
- 9.1. Introduction
- 9.2. Cash flows during a project
- 9.3. Project financing
- 9.4. Taxes and depreciation
- 9.5. Simple methods for economic analysis
- 9.6. Present value methods
- 9.7. Annualized cost methods
- 9.8. Sensitivity analysis
- 9.9. Project portfolio selection
- Chapter 10. Safety and loss prevention
- 10.1. Introduction
- 10.2. Materials hazards
- 10.3. Process hazards
- 10.4. Analysis of product and process safety
- 10.5. Failure mode effect analysis
- 10.6. Safety indices
- 10.7. Hazard and operability studies
- 10.8. Quantitative hazard analysis
- 10.9. Pressure relief
- Chapter 11. General site considerations
- 11.1. Introduction
- 11.2. Plant location and site selection
- 11.3. Site layout
- 11.4. Plant layout
- 11.5. Environmental considerations
- Chapter 12. Optimization in design
- 12.1. Introduction
- 12.2. The design objective
- 12.3. Constraints and degrees of freedom
- 12.4. Trade-offs
- 12.5. Problem decomposition
- 12.6. Optimization of a single decision variable
- 12.7. Search methods
- 12.8. Optimization of two or more decision variables
- 12.9. Linear programming
- 12.10. Nonlinear programming
- 12.11. Mixed-integer programming
- 12.12. Optimization in industrial practice
- II. Plant design
- Chapter 13. Equipment selection, specification, and design
- 13.1. Introduction
- 13.2. Sources of equipment design information
- 13.3. Guide to equipment selection and design
- Chapter 14. Design of pressure vessels
- 14.1. Introduction
- 14.2. Pressure vessel codes and standards
- 14.3. Fundamentals of strength of materials
- 14.4. General design considerations for pressure vessels
- 14.5. The design of thin-walled vessels under internal pressure
- 14.6. Compensation for openings and branches
- 14.7. Design of vessels subject to external pressure
- 14.8. Design of vessels subject to combined loading
- 14.9. Vessel supports
- 14.10. Bolted flanged joints
- 14.11. Welded joint design
- 14.12. Fatigue assessment of vessels
- 14.13. Pressure tests
- 14.14. High-pressure vessels
- 14.15. Liquid storage tanks
- 14.16. Capital cost of pressure vessels
- Chapter 15. Design of reactors and mixers
- 15.1. Introduction
- 15.2. Reactor design: General procedure
- 15.3. Sources of reaction engineering data
- 15.4. Choice of reaction conditions
- 15.5. Mixing
- 15.6. Heating and cooling of reacting systems
- 15.7. Multiphase reactors
- 15.8. Reactor design for catalytic processes
- 15.9. Design of bioreactors
- 15.10. Multifunctional batch reactors
- 15.11. Computer simulation of reactors
- 15.12. Determining actual reactor performance
- 15.13. Safety considerations in reactor design
- 15.14. Capital cost of reactors
- Chapter 16. Separation of fluids
- 16.1. Introduction
- 16.2. Gas–gas separations
- 16.3. Gas–liquid separators
- 16.4. Liquid–liquid separation
- 16.5. Separation of dissolved components
- Chapter 17. Separation columns (distillation, absorption, and extraction)
- 17.1. Introduction
- 17.2. Continuous distillation: Process description
- 17.3. Continuous distillation: Basic principles
- 17.4. Design variables in distillation
- 17.5. Design methods for binary systems
- 17.6. Multicomponent distillation: General considerations
- 17.7. Multicomponent distillation: Shortcut methods for stage and reflux requirements
- 17.8. Multicomponent distillation: Rigorous solution procedures (computer methods)
- 17.9. Other distillation processes
- 17.10. Plate efficiency
- 17.11. Approximate column sizing
- 17.12. Plate contactors
- 17.13. Plate hydraulic design
- 17.14. Packed columns
- 17.15. Column auxiliaries
- 17.16. Solvent extraction (liquid–liquid extraction)
- 17.17. Capital cost of separation columns
- Chapter 18. Specification and design of solids-handling equipment
- 18.1. Introduction
- 18.2. Properties of granular materials
- 18.3. Storage and transport of solids
- 18.4. Separation and mixing of solids
- 18.5. Gas–solids separations (gas cleaning)
- 18.6. Separation of solids from liquids
- 18.7. Separation of liquids from solids (drying)
- 18.8. Solids formation, shaping, and size enlargement processes
- 18.9. Particle size reduction (comminution)
- 18.10. Heat transfer to flowing solid particles
- 18.11. Hazards of solids processing
- Chapter 19. Heat transfer equipment
- 19.1. Introduction
- 19.2. Basic design procedure and theory
- 19.3. Overall heat transfer coefficient
- 19.4. Fouling factors (dirt factors)
- 19.5. Shell and tube exchangers: Construction details
- 19.6. Mean temperature difference (temperature driving force)
- 19.7. Shell and tube exchangers: General design considerations
- 19.8. Tube-side heat transfer coefficient and pressure drop (single phase)
- 19.9. Shell-side heat transfer and pressure drop (single phase)
- 19.10. Condensers
- 19.11. Reboilers and vaporizers
- 19.12. Plate heat exchangers
- 19.13. Direct-contact heat exchangers
- 19.14. Finned tubes
- 19.15. Double-pipe heat exchangers
- 19.16. Air-cooled exchangers
- 19.17. Fired heaters (furnaces and boilers)
- 19.18. Heat transfer to vessels
- 19.19. Capital cost of heat transfer equipment
- Chapter 20. Transport and storage of fluids
- 20.1. Introduction
- 20.2. Storage of fluids
- 20.3. Transport of gases and liquids
- 20.4. Pressure drop in pipelines
- 20.5. Valves
- 20.6. Compression and expansion of gases
- 20.7. Pumping of liquids
- 20.8. Selection of drivers for rotating equipment
- 20.9. Mechanical design of piping systems
- 20.10. Pipe size selection
- 20.11. Sizing of control valves
- Appendices
- Subject Index
- Edition: 3
- Published: July 14, 2021
- Imprint: Butterworth-Heinemann
- No. of pages: 1040
- Language: English
- Paperback ISBN: 9780128211793
- eBook ISBN: 9780323850483
GT
Gavin Towler
Gavin has 20 years of broad experience of process and product design and has 65 US patents. He is co-author of “Chemical Engineering Design”, a textbook on process design, and is an Adjunct Professor at Northwestern University, where he teaches the senior design classes.
Gavin has a B.A. and M.Eng. in chemical engineering from Cambridge University and a Ph.D. from U.C. Berkeley. He is a Chartered Engineer and Fellow of the Institute of Chemical Engineers, and is a Fellow of the AIChE.
RS
Ray Sinnott
After his career in industry he joined the Chemical Engineering Department, University of Wales Swansea in 1970, specialising in teaching process and plant design, and other engineering practice subjects.
The first edition of Chemical Engineering Design (Coulson and Richardson’s Vol 6) was published in 1983. Subsequent editions have been published at approximately 5 year intervals.
Ray Sinnott retired from full time teaching in 1995 but has maintained close contact with the engineering profession.