Product and Process Design Principles: Synthesis, Analysis, and Evaluation, 4th Edition, EMEA Edition

Name: Product and Process Design Principles: Synthesis, Analysis, and Evaluation, 4th Edition, EMEA Edition
Price: 4790 ISK
Availability: InStock
Author: Warren D. Seider; Daniel R. Lewin; J. D. Seader; Soemantri Widagdo; Rafiqul Gani; Ka Ming Ng
ISBN: 9781119636960

Höfundar: Warren D. Seider; Daniel R. Lewin; J. D. Seader; Soemantri Widagdo; Rafiqul Gani; Ka Ming Ng (Útgáfa: 4)

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The new 4th 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.

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Útgefandi: Wiley Global Education UK

ISBN: 9781119636960

Print ISBN: 9781119588009

Format: ePub

Útgáfa: 4

Höfundar: Warren D. Seider; Daniel R. Lewin; J. D. Seader; Soemantri Widagdo; Rafiqul Gani; Ka Ming Ng

Tungumál: English

Útgefið: 2019-12-12

Prent takmörkun á líftíma: 100

Prent takmörkun: 10

Afritunar takmörkun: 2

Flokkar: Verkfræði

Efnisflokkar: Tækni og verkfræði › Efna- og lífefnafræði

Kaflar

COVER
TITLE PAGE
ABOUT THE AUTHORS
PREFACE
OBJECTIVES
LIMITED TIME—PROCESS OR PRODUCT DESIGN?
FORMAT OF COURSEWARE AND SUPPORTING WEB SITE
ADVICE TO STUDENTS AND INSTRUCTORS
ACKNOWLEDGMENTS
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
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
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
NOTE
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
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
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
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
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
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
CHAPTER 14 PUMPS, COMPRESSORS, AND EXPANDERS
14.0 OBJECTIVES
14.1 PUMPS
14.2 COMPRESSORS AND EXPANDERS
14.3 SUMMARY
REFERENCES
EXERCISES
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
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
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
PART THREE DESIGN ANALYSIS—PRODUCT AND PROCESS
CHAPTER 18 SIX-SIGMA DESIGN STRATEGIES
18.0 OBJECTIVES
18.1 INTRODUCTION
18.2 SIX-SIGMA METHODOLOGY IN PRODUCT DESIGN AND MANUFACTURING
18.3 EXAMPLE APPLICATIONS
18S Penicillin Plant Fermenter and Extraction Models
18.4 SUMMARY
REFERENCES
EXERCISES
CHAPTER 19 BUSINESS DECISION MAKING IN PRODUCT DEVELOPMENT
19.0 OBJECTIVES
19.1 INTRODUCTION
19.2 ECONOMIC ANALYSIS
19.3 MAKE-OR-BUY DECISIONS
19.4 MICROECONOMICS OF PRODUCT DEVELOPMENT
19.5 COMPANY AND SOCIETAL FACTORS AFFECTING PRODUCT DEVELOPMENT
19.6 SUMMARY
REFERENCES
EXERCISES
CHAPTER 20 PLANTWIDE CONTROLLABILITY ASSESSMENT
20.0 OBJECTIVES
20.1 INTRODUCTION
20.2 CONTROL SYSTEM CONFIGURATION
20.3 QUALITATIVE PLANTWIDE CONTROL SYSTEM SYNTHESIS
20.4 SUMMARY
20S Flowsheet Controllability Analysis
REFERENCES
EXERCISES
CHAPTER 21 DESIGN OPTIMIZATION
21.0 OBJECTIVES
21.1 INTRODUCTION
21.2 GENERAL FORMULATION OF THE OPTIMIZATION PROBLEM
21.3 CLASSIFICATION OF OPTIMIZATION PROBLEMS
21.4 LINEAR PROGRAMMING (LP)
21.5 NONLINEAR PROGRAMMING (NLP) WITH A SINGLE VARIABLE
21.6 CONDITIONS FOR NONLINEAR PROGRAMMING (NLP) BY GRADIENT METHODS WITH TWO OR MORE DECISION VARIABLES
21.7 OPTIMIZATION ALGORITHM
21.8 FLOWSHEET OPTIMIZATIONS—CASE STUDIES
21.9 SUMMARY
REFERENCES
EXERCISES
CHAPTER 22 OPTIMAL DESIGN AND SCHEDULING OF BATCH PROCESSES
22.0 OBJECTIVES
22.1 INTRODUCTION
22.2 DESIGN OF BATCH PROCESS UNITS
22.3 DESIGN OF REACTOR–SEPARATOR PROCESSES
22.4 DESIGN OF SINGLE-PRODUCT PROCESSING SEQUENCES
22.5 DESIGN ON MULTIPRODUCT PROCESSING SEQUENCES
22.6 SUMMARY
REFERENCES
EXERCISES
PART FOUR DESIGN REPORTS—PRODUCT AND PROCESS
CHAPTER 23 WRITTEN REPORTS AND ORAL PRESENTATIONS
23.0 OBJECTIVES
23.1 CONTENTS OF THE WRITTEN REPORT
23.2 PREPARATION OF THE WRITTEN REPORT
23.3 ORAL DESIGN PRESENTATIONS
23.4 AWARD COMPETITION
23.5 SUMMARY
REFERENCES
PART FIVE CASE STUDIES—PRODUCT AND PROCESS DESIGNS
CHAPTER 24 CASE STUDY 1—HOME HEMODIALYSIS DEVICES
24.0 OBJECTIVES
24.1 HEMODIALYSIS TECHNOLOGY
24.2 DESIGN SPECIFICATIONS OF HOME HEMODIALYSIS DEVICE
24.3 SUMMARY
REFERENCES
PATENTS—HEMODIALYSIS DEVICES—HOLLOW-FIBER MEMBRANES
PATENTS—HEMODIALYSIS DEVICES—DIALYSATE REGENERATION
PATENTS—HEMODIALYSIS DEVICES—ALARMS/USER INTERFACE
EXERCISES
CHAPTER 25 CASE STUDY 2—HIGH THROUGHPUT SCREENING DEVICES FOR KINASE INHIBITORS
25.0 OBJECTIVES
25.1 BACKGROUND TECHNOLOGY FOR HIGH THROUGHPUT SCREENING OF KINASE INHIBITORS
25.2 PRODUCT CONCEPT
25.3 PROTOTYPING
25.4 PRODUCT DEVELOPMENT
25.5 SUMMARY
REFERENCES
PATENTS
EXERCISES
CHAPTER 26 CASE STUDY 3—DIE ATTACH ADHESIVE: A CASE STUDY OF PRODUCT DEVELOPMENT
26.0 OBJECTIVES
26.1 BACKGROUND OF TECHNOLOGY
26.2 MARKET STUDY
26.3 PRODUCT DESIGN
26.4 PROCESS DESIGN
26.5 PROTOTYPING
26.6 ESTIMATION OF PRODUCT COST
26.7 SUMMARY
REFERENCES
EXERCISES
CHAPTER 27 CASE STUDY 4—AMMONIA PROCESS
27.0 OBJECTIVES
27.1 INTRODUCTION
27.2 INITIAL BASE CASE DESIGN
27.3 DESIGN REFINEMENT
REFERENCES
EXERCISES
NOTE
CHAPTER 28 CASE STUDY 5—WINE AERATOR DEVICE
CHAPTER 29 CASE STUDY 6—FAUCET WATER PURIFIER
CHAPTER 30 CASE STUDY 7—DOMESTIC DEHUMIDIFIER
CHAPTER 31 CASE STUDY 8—VITAMIN C TABLETS
CHAPTER 32 CASE STUDY 9—CONDUCTIVE INK FOR PRINTED ELECTRONICS
CHAPTER 33 CASE STUDY 10—PVB INTERLAYER FOR SMART WINDOW
APPENDIX I RESIDUE CURVES FOR HETEROGENEOUS SYSTEMS
APPENDIX II DESIGN PROBLEM STATEMENTS BY AREA
APPENDIX III MATERIALS OF CONSTRUCTION
TABLE OF ACRONYMS
AUTHOR INDEX
SUBJECT INDEX
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