Title Page
by Debangsu Bhattacharyya, Joseph A. Shaeiwitz, Wallace B. Whiting, Richard C. Bail
Analysis, Synthesis, and Design of Chemical Processes, Fourth Edition
- Title Page
- Copyright Page
- Contents
- Material on the CD-ROM
- Preface
- About the Authors
- List of Nomenclature
- Section I. Conceptualization and Analysis of Chemical Processes
- Chapter 1. Diagrams for Understanding Chemical Processes
- 1.1. Block Flow Diagram (BFD)
- 1.2. Process Flow Diagram (PFD)
- 1.3. Piping and Instrumentation Diagram (P&ID)
- 1.4. Additional Diagrams
- 1.5. Three-Dimensional Representation of a Process
- 1.6. The 3-D Plant Model
- 1.7. Operator and 3-D Immersive Training Simulators
- 1.8. Summary
- References
- Short Answer Questions
- Problems
- Chapter 2. The Structure and Synthesis of Process Flow Diagrams
- 2.1. Hierarchy of Process Design
- 2.2. Step 1—Batch Versus Continuous Process
- 2.3. Step 2—The Input/Output Structure of the Process
- 2.4. Step 3—The Recycle Structure of the Process
- 2.5. Step 4—General Structure of the Separation System
- 2.6. Step 5—Heat-Exchanger Network or Process Energy Recovery System
- 2.7. Information Required and Sources
- 2.8. Summary
- References
- Short Answer Questions
- Problems
- Chapter 3. Batch Processing
- 3.1. Design Calculations for Batch Processes
- 3.2. Gantt Charts and Scheduling
- 3.3. Nonoverlapping Operations, Overlapping Operations, and Cycle Times
- 3.4. Flowshop and Jobshop Plants
- 3.5. Product and Intermediate Storage and Parallel Process Units
- 3.6. Design of Equipment for Multiproduct Batch Processes
- 3.7. Summary
- References
- Short Answer Questions
- Problems
- Chapter 4. Chemical Product Design
- Chapter 5. Tracing Chemicals through the Process Flow Diagram
- Chapter 6. Understanding Process Conditions
- 6.1. Conditions of Special Concern for the Operation of Separation and Reactor Systems
- 6.2. Reasons for Operating at Conditions of Special Concern
- 6.3. Conditions of Special Concern for the Operation of Other Equipment
- 6.4. Analysis of Important Process Conditions
- 6.5. Summary
- References
- Short Answer Questions
- Problems
- Chapter 1. Diagrams for Understanding Chemical Processes
- Section II. Engineering Economic Analysis of Chemical Processes
- Chapter 7. Estimation of Capital Costs
- Chapter 8. Estimation of Manufacturing Costs
- 8.1. Factors Affecting the Cost of Manufacturing a Chemical Product
- 8.2. Cost of Operating Labor
- 8.3. Utility Costs
- 8.4. Raw Material Costs
- 8.5. Yearly Costs and Stream Factors
- 8.6. Estimating Utility Costs from the PFD
- 8.7. Cost of Treating Liquid and Solid Waste Streams
- 8.8. Evaluation of Cost of Manufacture for the Production of Benzene Via the Hydrodealkylation of Toluene
- 8.9. Summary
- References
- Short Answer Questions
- Problems
- Chapter 9. Engineering Economic Analysis
- 9.1. Investments and the Time Value of Money
- 9.2. Different Types of Interest
- 9.3. Time Basis for Compound Interest Calculations
- 9.4. Cash Flow Diagrams
- 9.5. Calculations from Cash Flow Diagrams
- 9.6. Inflation
- 9.7. Depreciation of Capital Investment
- 9.8. Taxation, Cash Flow, and Profit
- 9.9. Summary
- References
- Short Answer Questions
- Problems
- Chapter 10. Profitability Analysis
- 10.1. A Typical Cash Flow Diagram for a New Project
- 10.2. Profitability Criteria for Project Evaluation
- 10.3. Comparing Several Large Projects: Incremental Economic Analysis
- 10.4. Establishing Acceptable Returns from Investments: The Concept of Risk
- 10.5. Evaluation of Equipment Alternatives
- 10.6. Incremental Analysis for Retrofitting Facilities
- 10.7. Evaluation of Risk in Evaluating Profitability
- 10.8. Profit Margin Analysis
- 10.9. Summary
- References
- Short Answer Questions
- Problems
- Section III. Synthesis and Optimization of Chemical Processes
- Chapter 11. Utilizing Experience-Based Principles to Confirm the Suitability of a Process Design
- Chapter 12. Synthesis of the PFD from the Generic BFD
- 12.1. Information Needs and Sources
- 12.2. Reactor Section
- 12.3. Separator Section
- 12.4. Reactor Feed Preparation and Separator Feed Preparation Sections
- 12.5. Recycle Section
- 12.6. Environmental Control Section
- 12.7. Major Process Control Loops
- 12.8. Flow Summary Table
- 12.9. Major Equipment Summary Table
- 12.10. Summary
- References
- General Reference
- Problems
- Chapter 13. Synthesis of a Process Using a Simulator and Simulator Troubleshooting
- 13.1. The Structure of a Process Simulator
- 13.2. Information Required to Complete a Process Simulation: Input Data
- 13.3. Handling Recycle Streams
- 13.4. Choosing Thermodynamic Models
- 13.5. Case Study: Toluene Hydrodealkylation Process
- 13.6. Electrolyte Systems Modeling
- 13.7. Solids Modeling
- Appendix 13.1. Calculation of Excess Gibbs Energy for Electrolyte Systems
- Appendix 13.2. Steps to Build a Model of a Distillation Column for an Electrolyte System Using a Rate-Based Simulation with a Film Model for Mass Transfer, the Parameters Required at Each Stage, and P
- 13.8. Summary
- References
- Short Answer Questions
- Problems
- Chapter 14. Process Optimization
- 14.1. Background Information on Optimization
- 14.2. Strategies
- 14.3. Topological Optimization
- 14.4. Parametric Optimization
- 14.5. Lattice Search Techniques versus Response Surface Techniques
- 14.6. Process Flexibility and the Sensitivity of the Optimum
- 14.7. Optimization in Batch Systems
- 14.8. Summary
- References
- Short Answer Questions
- Problems
- Chapter 15. Pinch Technology
- 15.1. Introduction
- 15.2. Heat Integration and Network Design
- 15.3. Composite Temperature-Enthalpy Diagram
- 15.4. Composite Enthalpy Curves for Systems without a Pinch
- 15.5. Using the Composite Enthalpy Curve to Estimate Heat-Exchanger Surface Area
- 15.6. Effectiveness Factor (F) and the Number of Shells
- 15.7. Combining Costs to Give the Eaoc for the Network
- 15.8. Other Considerations
- 15.9. Heat-Exchanger Network Synthesis Analysis and Design (HENSAD) Program
- 15.10. Mass-Exchange Networks
- 15.11. Summary
- References
- Short Answer Questions
- Problems
- Chapter 16. Advanced Topics Using Steady-State Simulators
- Chapter 17. Using Dynamic Simulators in Process Design
- Chapter 18. Regulation and Control of Chemical Processes with Applications Using Commercial Software
- 18.1. A Simple Regulation Problem
- 18.2. The Characteristics of Regulating Valves
- 18.3. Regulating Flowrates and Pressures
- 18.4. The Measurement of Process Variables
- 18.5. Common Control Strategies Used in Chemical Processes
- 18.6. Exchanging Heat and Work Between Process and Utility Streams
- 18.7. Logic Control
- 18.8. Advanced Process Control
- 18.9. Case Studies
- 18.10. Putting it all Together: The Operator Training Simulator (OTS)
- 18.11. Summary
- References
- Problems
- Section IV. Analysis of Process Performance
- Section V. The Impact of Chemical Engineering Design on Society
- Chapter 25. Ethics and Professionalism
- Chapter 26. Health, Safety, and the Environment
- Chapter 27. Green Engineering
- 27.1. Environmental Regulations
- 27.2. Environmental Fate of Chemicals
- 27.3. Green Chemistry
- 27.4. Pollution Prevention During Process Design
- 27.5. Analysis of a PFD for Pollution Performance and Environmental Performance
- 27.6. An Example of the Economics of Pollution Prevention
- 27.7. Life Cycle Analysis
- 27.8. Summary
- References
- Problems
- Section VI. Interpersonal and Communication Skills
- Appendix A. Cost Equations and Curves for the CAPCOST Program
- Index
- Chapter 0. Outcomes Assessment
- Chapter 29. Written and Oral Communication
- Chapter 30. A Report-Writing Case Study
- Appendix B. Information for the Preliminary Design of Fifteen Chemical Processes
- B.1. Dimethyl Ether (DME) Production, Unit 200
- B.2. Ethylbenzene Production, Unit 300
- B.3. Styrene Production, Unit 400
- B.4. Drying Oil Production, Unit 500
- B.5. Production Of Maleic Anhydride From Benzene, Unit 600
- B.6. Ethylene Oxide Production, Unit 700
- B.7. Formalin Production, Unit 800
- B.8. Batch Production Of L-Phenylalanine And L-Aspartic Acid, Unit 900
- B.9. Acrylic Acid Production Via The Catalytic Partial Oxidation Of Propylene [1, 2, 3, 4, 5], Unit 1000
- B.10. Production Of Acetone Via The Dehydrogenation Of Isopropyl Alcohol (IPA) [1, 2, 3, 4], Unit 1100
- B.11. Production Of Heptenes From Propylene And Butenes [1], Unit 1200
- B.12. Design of a Shift Reactor Unit to Convert Co To Co2, Unit 1300
- B.13. Design of a Dual-Stage Selexol Unit to Remove CO2 And H2S From Coal-Derived Synthesis Gas, Unit 1400
- B.14. Design of a Claus Unit For the Conversion of H2s to Elemental Sulfur, Unit 1500
- B.15. Modeling a Downward-Flow, Oxygen-Blown, Entrained-Flow Gasifier, Unit 1600
- Appendix C. Design Projects
- Project 1. Increasing the Production of 3-Chloro-1-Propene (Allyl Chloride) in Unit 600
- PROJECT 2. Design and Optimization of a New 20,000-Metric-Tons-per-Year Facility to Produce Allyl Chloride at La Nueva Cantina, Mexico
- PROJECT 3. Scale-Down of Phthalic Anhydride Production at TBWS Unit 700
- PROJECT 4. The Design of a New 100,000-Metric-Tons-per-Year Phthalic Anhydride Production Facility
- PROJECT 5. Problems at the Cumene Production Facility, Unit 800
- PROJECT 6. Design of a New, 100,000-Metric-Tons-per-Year Cumene Production Facility
- Where are the Companion Content Files?
Analysis, Synthesis, and Design of Chemical Processes
Fourth Edition
Richard Turton
Richard C. Bailie
Wallace B. Whiting
Joseph A. Shaeiwitz
Debangsu Bhattacharyya
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