Product and Process Design Principles Synthesis Analysis 4th edition by Warren Seider, Daniel Lewin, Seader, Soemantri Widagdo, Rafiqul Gani, Ka Ming Ng ISBN 1119475260 9781119475262

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ISBN 10: 1119475260
ISBN 13: 9781119475262
Author: Warren Seider, Daniel Lewin, Seader, Soemantri Widagdo, Rafiqul Gani, Ka Ming Ng

The new 4^th edition of Seider’s Product and Process Design Principles: Synthesis, Analysis and Design covers content for process design courses in the chemical engineering curriculum, showing how process design and product design are inter-linked and why studying the two is important for modern applications. A principal objective of this new edition is to describe modern strategies for the design of chemical products and processes, with an emphasis on a systematic approach. This fourth edition presents two parallel tracks: (1) product design, and (2) process design, with an emphasis on process design. Process design instructors can show easily how product designs lead to new chemical processes. Alternatively, product design can be taught in a separate course subsequent to the process design course.

Product and Process Design Principles Synthesis Analysis 4th Table of contents:

PART ONE: INTRODUCTION TO PRODUCT AND PROCESS DESIGN

CHAPTER 1: INTRODUCTION TO CHEMICAL PRODUCT DESIGN
1.0 OBJECTIVES
1.1 INTRODUCTION
1.2 THE DIVERSITY OF CHEMICAL PRODUCTS
1.3 PRODUCT DESIGN AND DEVELOPMENT
1.4 SUMMARY
REFERENCES
EXERCISES

CHAPTER 2: INTRODUCTION TO PROCESS DESIGN
2.0 OBJECTIVES
2.1 INTRODUCTION
2.2 EXPERIMENTS
2.3 PRELIMINARY PROCESS SYNTHESIS
2.4 NEXT PROCESS DESIGN TASKS
2.5 PRELIMINARY FLOWSHEET MASS BALANCES
2.6 SUMMARY
REFERENCES
EXERCISES

CHAPTER 3: DESIGN LITERATURE, STIMULATING INNOVATION, ENERGY, ENVIRONMENT, SUSTAINABILITY, SAFETY, ENGINEERING ETHICS
3.0 OBJECTIVES
3.1 DESIGN LITERATURE
3.2 STIMULATING INVENTION AND INNOVATION
3.3 ENERGY SOURCES
3.4 ENVIRONMENTAL PROTECTION
3.5 SUSTAINABILITY
3.6 SAFETY CONSIDERATIONS
3.7 ENGINEERING ETHICS
3.8 SUMMARY
REFERENCES
EXERCISES

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PART TWO: DESIGN SYNTHESIS—PRODUCT AND PROCESSES

CHAPTER 4: MOLECULAR AND MIXTURE DESIGN
4.0 OBJECTIVES
4.1 INTRODUCTION
4.2 FRAMEWORK FOR COMPUTER-AIDED MOLECULAR-MIXTURE DESIGN
4S-1 Liquid Blend Product Design
4S-2 Formulated Liquid Product Design
4S-3 Software for Molecular and Mixture Design
4.3 CASE STUDIES
4.4 SUMMARY
REFERENCES
EXERCISES

CHAPTER 5: DESIGN OF CHEMICAL DEVICES, FUNCTIONAL PRODUCTS, AND FORMULATED PRODUCTS
5.0 OBJECTIVES
5.1 INTRODUCTION
5.2 DESIGN OF CHEMICAL DEVICES AND FUNCTIONAL PRODUCTS
5.3 DESIGN OF FORMULATED PRODUCTS
5.4 DESIGN OF PROCESSES FOR B2C PRODUCTS
5.5 SUMMARY
REFERENCES
EXERCISES

CHAPTER 6: HEURISTICS FOR PROCESS SYNTHESIS
6.0 OBJECTIVES
6S-0 Introduction to Three Supplements for Chapter 6
6S-1 Hybrid Process-Group Based Process Synthesis
6S-2 Math Programming Superstructures for Process Synthesis
6S-3 ProCAFD, Computer-Aided Flowsheet Design
6.1 INTRODUCTION
6.2 RAW MATERIALS AND CHEMICAL REACTIONS
6.3 DISTRIBUTION OF CHEMICALS
6.4 SEPARATIONS
6.5 HEAT REMOVAL FROM AND ADDITION TO REACTORS
6.6 HEAT EXCHANGERS AND FURNACES
6.7 PUMPING, COMPRESSION, PRESSURE REDUCTION, VACUUM, AND CONVEYING OF SOLIDS
6.8 CHANGING THE PARTICLE SIZE OF SOLIDS AND SIZE SEPARATION OF PARTICLES
6.9 REMOVAL OF PARTICLES FROM GASES AND LIQUIDS
6.10 CONSIDERATIONS THAT APPLY TO THE ENTIRE FLOWSHEET
6.11 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 7: SIMULATION TO ASSIST IN PROCESS CREATION
7.0 OBJECTIVES
7.1 INTRODUCTION
7.2 PRINCIPLES OF PROCESS SIMULATION
7.3 PROCESS CREATION THROUGH PROCESS SIMULATION
7.4 CASE STUDIES
7.5 PRINCIPLES OF BATCH FLOWSHEET SIMULATION
7.6 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 8: SYNTHESIS OF NETWORKS CONTAINING REACTORS
8.0 OBJECTIVES
8.1 INTRODUCTION
8.2 REACTOR MODELS IN THE PROCESS SIMULATORS
8.3 REACTOR NETWORK DESIGN USING THE ATTAINABLE REGION
8.4 REACTOR DESIGN FOR COMPLEX CONFIGURATIONS
8.5 LOCATING THE SEPARATION SECTION WITH RESPECT TO THE REACTOR SECTION
8.6 TRADE-OFFS IN PROCESSES INVOLVING RECYCLE
8.7 OPTIMAL REACTOR CONVERSION
8.8 RECYCLE TO EXTINCTION
8.9 SNOWBALL EFFECTS IN THE CONTROL OF PROCESSES INVOLVING RECYCLE
8.10 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 9: SYNTHESIS OF SEPARATION TRAINS
9.0 OBJECTIVES
9.1 INTRODUCTION
9.2 CRITERIA FOR SELECTION OF SEPARATION METHODS
9.3 SELECTION OF EQUIPMENT
9.4 SEQUENCING OF ORDINARY DISTILLATION COLUMNS FOR THE SEPARATION OF NEARLY IDEAL LIQUID MIXTURES
9.5 SEQUENCING OF OPERATIONS FOR THE SEPARATION OF NONIDEAL LIQUID MIXTURES
9.6 SEPARATION SYSTEMS FOR GAS MIXTURES
9.7 SEPARATION SYSTEMS FOR SOLID-FLUID MIXTURES
9.8 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 10: SECOND-LAW ANALYSIS
10.0 OBJECTIVES
10.1 INTRODUCTION
10.2 THE SYSTEM AND THE SURROUNDINGS
10.3 ENERGY TRANSFER
10.4 THERMODYNAMIC PROPERTIES
10.5 EQUATIONS FOR SECOND-LAW ANALYSIS
10.6 EXAMPLES OF LOST-WORK CALCULATIONS
10.7 THERMODYNAMIC EFFICIENCY
10.8 CAUSES OF LOST WORK
10.9 THREE EXAMPLES OF SECOND-LAW ANALYSIS
10.10 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 11: HEAT AND POWER INTEGRATION
11.0 OBJECTIVES
11.1 INTRODUCTION
11.2 MINIMUM UTILITY TARGETS
11.3 NETWORKS FOR MAXIMUM ENERGY RECOVERY
11.4 MINIMUM NUMBER OF HEAT EXCHANGERS
11.5 THRESHOLD APPROACH TEMPERATURE
11.6 OPTIMUM APPROACH TEMPERATURE
11.7 MULTIPLE UTILITIES
11.8 HEAT-INTEGRATED REACTORS AND DISTILLATION TRAINS
11.9 HEAT ENGINES AND HEAT PUMPS
11.10 SUMMARY
11S-1 MILP and MINLP Applications in HEN Synthesis
11S-2 Mass Integration
REFERENCES
EXERCISES

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CHAPTER 12: HEAT EXCHANGER DESIGN
12.0 OBJECTIVES
12.1 INTRODUCTION
12.2 EQUIPMENT FOR HEAT EXCHANGE
12.3 HEAT-TRANSFER COEFFICIENTS AND PRESSURE DROP
12.4 DESIGN OF SHELL-AND-TUBE HEAT EXCHANGERS
12.5 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 13: SEPARATION TOWER DESIGN
13.0 OBJECTIVES
13.1 OPERATING CONDITIONS
13.2 FENSKE-UNDERWOOD-GILLILAND (FUG) SHORTCUT METHOD FOR ORDINARY DISTILLATION
13.3 KREMSER SHORTCUT METHOD FOR ABSORPTION AND STRIPPING
13.4 RIGOROUS MULTICOMPONENT, MULTIEQUILIBRIUM-STAGE METHODS WITH A SIMULATOR
13.5 PLATE EFFICIENCY AND HETP
13.6 TOWER DIAMETER
13.7 PRESSURE DROP AND WEEPING
13.8 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 14: PUMPS, COMPRESSORS, AND EXPANDERS
14.0 OBJECTIVES
14.1 PUMPS
14.2 COMPRESSORS AND EXPANDERS
14.3 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 15: CHEMICAL REACTOR DESIGN
15.0 OBJECTIVES
15.1 INTRODUCTION
15.2 LIMITING APPROXIMATE MODELS FOR TUBULAR REACTORS
15.3 THE COMSOL CFD PACKAGE
15.4 CFD FOR TUBULAR REACTOR MODELS
15.5 NONISOTHERMAL TUBULAR REACTOR MODELS
15.6 MIXING IN STIRRED-TANK REACTORS
15.7 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 16: COST ACCOUNTING AND CAPITAL COST ESTIMATION
16.0 OBJECTIVES
16.1 ACCOUNTING
16.2 COST INDEXES AND CAPITAL INVESTMENT
16.3 CAPITAL INVESTMENT COSTS
16.4 ESTIMATION OF THE TOTAL CAPITAL INVESTMENT
16.5 PURCHASE COSTS OF THE MOST WIDELY USED PROCESS EQUIPMENT
16.6 PURCHASE COSTS OF OTHER CHEMICAL PROCESSING EQUIPMENT
16.7 EQUIPMENT COSTING SPREADSHEET
16.8 EQUIPMENT SIZING AND CAPITAL COST ESTIMATION USING ASPEN PROCESS ECONOMIC ANALYZER (APEA)
16.9 SUMMARY
REFERENCES
EXERCISES

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CHAPTER 17: ANNUAL COSTS, EARNINGS, AND PROFITABILITY ANALYSIS
17.0 OBJECTIVES
17.1 INTRODUCTION
17.2 ANNUAL SALES REVENUES, PRODUCTION COSTS, AND THE COST SHEET
17.3 WORKING CAPITAL AND TOTAL CAPITAL INVESTMENT
17.4 APPROXIMATE PROFITABILITY MEASURES
17.5 TIME VALUE OF MONEY
17.6 CASH FLOW AND DEPRECIATION
17.7 RIGOROUS PROFITABILITY MEASURES
17.8 PROFITABILITY ANALYSIS SPREADSHEET
17.9 SUMMARY
REFERENCES
EXERCISES

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Tags: Warren Seider, Daniel Lewin, Seader, Soemantri Widagdo, Rafiqul Gani, Ka Ming Ng, Process Design, Synthesis Analysis