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Warren D. Seider is Professor of Chemical Engineering at the University of Pennsylvania. He received a B.S. degree from the Polytechnic Institute of Brooklyn and M.S. and Ph.D. degrees from the University of Michigan. Seider has contributed to the fields of process analysis, simulation, design, and control. He has authored or coauthored over 110 journal articles and authored or edited seven books. He helped to organize the CACHE (Computer Aids for Chemical Engineering Education) Committee in 1969 and served as its chairman. Seider is a member of the Editorial Advisory Board of Computers and Chemical Engineering.
Daniel R. Lewin is Professor of Chemical Engineering, the Churchill Family Chair, and the Director of the Process Systems Engineering (PSE) research group at the Technion, the Israel Institute of Technology. He received his [...]. from the University of Edinburgh and his [...]. from the Technion. He has authored or co-authored over 100 technical publications in the area of process systems engineering, as well as the first three editions of this textbook, and the multimedia CD that accompanies it.
J. D. Seader is Professor Emeritus of Chemical Engineering at the University of Utah. He received B.S. and M.S. degrees from the University of California at Berkeley and a Ph.D. from the University of Wisconsin. In 2004, he received, with Professor Warren D. Seider, the Warren K. Lewis Award for Chemical Engineering Education from the AIChE. In 2008, his textbook, "Separation Process Principles" with co-author Ernest J. Henley, was cited as one of 30 ground-breaking books in the last 100 years of chemical engineering.
Soemantri Widagdo is a retired R&D executive after a 15-year career at 3M. His last position was the R&D Head of 3M Southeast Asia. He received his B.S. degree in chemical engineering from Bandung Institute of Technology, Indonesia, and his [...].E. and Ph.D. degrees from Stevens Institute of Technology. He has been involved in a variety of technology and product-development programs involving renewable energy, industrial and transportation applications, consumer office products, electrical and electronics applications, health care and dentistry, and display and graphics applications. He has authored and co-authored over 20 technical publications and two patents.
Rafiqul Gani is Professor of System Design at the Department of Chemical & Biochemical Engineering, The Technical University of Denmark and the head and co-founder of the Computer Aided Product-Process Engineering Center (CAPEC). He received a B.S degree from the Bangladesh University of Engineering and Technology, and M.S., DIC and Ph.D. degrees from Imperial College, London. He has published more than 200 peer-reviewed journal articles and delivered over 300 lectures, seminars and plenary/keynote lectures at international conferences, institutions and companies all over the world. Professor Gani is currently (2014-2016) the president of the EFCE (European Federation of Chemical Engineering); a member of the Board of Trustees of the AIChE; a Fellow of the AIChE and also a Fellow of IChemE.
Ka Ming Ng is Chair Professor of Chemical and Biomolecular Engineering at the Hong Kong University of Science and Technology. He obtained his B.S. degree from the University of Minnesota and his Ph.D. from the University of Houston. His research interests center on product conceptualization, process design and business development involving water, natural herbs, nanomaterials, and advanced materials. He is a fellow of the American Institute of Chemical Engineers where he received the Excellence in Process Development Research Award in 2002.
PART ONE INTRODUCTION TO PRODUCT AND PROCESS DESIGN 1
Chapter 1 Introduction to Chemical Product Design 3
1.0 Objectives 3
1.1 Introduction 3
1.2 The Diversity of Chemical Products 3
1.3 Product Design and Development 7
1.4 Summary 16
References 17
Exercises 17
Chapter 2 Introduction to Process Design 19
2.0 Objectives 19
2.1 Introduction 19
2.2 Experiments 21
2.3 Preliminary Process Synthesis 21
2.4 Next Process Design Tasks 40
2.5 Preliminary Flowsheet Mass Balances 41
2.6 Summary 45
References 45
Exercises 45
Chapter 3 Design Literature, Stimulating Innovation, Energy, Environment, Sustainability, Safety, Engineering Ethics 47
3.0 Objectives 47
3.1 Design Literature 47
3.2 Stimulating Invention and Innovation 50
3.3 Energy Sources 51
3.4 Environmental Protection 56
3.5 Sustainability 60
3.6 Safety Considerations 63
3.7 Engineering Ethics 70
3.8 Summary 73
References 73
Exercises 74
3S Supplement to Chapter 3-NSPE Code of Ethics (Online [...]
PART TWO DESIGN SYNTHESIS-PRODUCT AND PROCESSES 77
Chapter 4 Molecular and Mixture Design 79
4.0 Objectives 79
4.1 Introduction 79
4.2 Framework for Computer-Aided Molecular-Mixture Design 81
4.3 Case Studies 98
4.4 Summary 107
References 107
Exercises 108
Chapter 5 Design of Chemical Devices, Functional Products, and Formulated Products 110
5.0 Objectives 110
5.1 Introduction 110
5.2 Design of Chemical Devices and Functional Products 112
5.3 Design of Formulated Products 117
5.4 Design of Processes for B2C Products 123
5.5 Summary 126
References 127
Exercises 127
Chapter 6 Heuristics for Process Synthesis 132
6.0 Objectives 132
6.1 Introduction 133
6.2 Raw Materials and Chemical Reactions 133
6.3 Distribution of Chemicals 135
6.4 Separations 141
6.5 Heat Removal From and Addition to Reactors 145
6.6 Heat Exchangers and Furnaces 148
6.7 Pumping, Compression, Pressure Reduction, Vacuum, and Conveying of Solids 150
6.8 Changing the Particle Size of Solids and Size Separation of Particles 153
6.9 Removal of Particles From Gases and Liquids 154
6.10 Considerations that Apply to the Entire Flowsheet 154
6.11 Summary 155
References 159
Exercises 160
Chapter 7 Simulation to Assist in Process Creation 162
7.0 Objectives 162
7.1 Introduction 162
7.2 Principles of Process Simulation 163
7.3 Process Creation through Process Simulation 176
7.4 Case Studies 184
7.5 Principles of Batch Flowsheet Simulation 194
7.6 Summary 201
References 202
Exercises 202
Chapter 8 Synthesis of Networks Containing Reactors 209
8.0 Objectives 209
8.1 Introduction 209
8.2 Reactor Models in the Process Simulators 210
8.3 Reactor Network Design Using the Attainable Region 215
8.4 Reactor Design for Complex Configurations 220
8.5 Locating the Separation Section with Respect to the Reactor Section 224
8.6 Trade-Offs in Processes Involving Recycle 227
8.7 Optimal Reactor Conversion 228
8.8 Recycle to Extinction 229
8.9 Snowball Effects in the Control of Processes Involving Recycle 231
8.10 Summary 231
References 232
Exercises 232
Chapter 9 Synthesis of Separation Trains 234
9.0 Objectives 234
9.1 Introduction 234
9.2 Criteria for Selection of Separation Methods 241
9.3 Selection of Equipment 244
9.4 Sequencing of Ordinary Distillation Columns for the Separation of Nearly Ideal Liquid Mixtures 245
9.5 Sequencing of Operations for the Separation of Nonideal Liquid Mixtures 257
9.6 Separation Systems for Gas Mixtures 277
9.7 Separation Systems for Solid-Fluid Mixtures 279
9.8 Summary 280
References 280
Exercises 282
Chapter 10 Second-Law Analysis 287
10.0 Objectives 287
10.1 Introduction 287
10.2 The System and the Surroundings 289
10.3 Energy Transfer 289
10.4 Thermodynamic Properties 290
10.5 Equations for Second-Law Analysis 295
10.6 Examples of Lost-Work Calculations 297
10.7 Thermodynamic Efficiency 299
10.8 Causes of Lost Work 300
10.9 Three Examples of Second-Law Analysis 300
10.10 Summary 310
References 310
Exercises 310
Chapter 11 Heat and Power Integration 316
11.0 Objectives 316
11.1 Introduction 316
11.2 Minimum Utility Targets 319
11.3 Networks for Maximum Energy Recovery 325
11.4 Minimum Number of Heat Exchangers 329
11.5 Threshold Approach Temperature 334
11.6 Optimum Approach Temperature 336
11.7 Multiple Utilities 337
11.8 Heat-Integrated Reactors and Distillation Trains 342
11.9 Heat Engines and Heat Pumps 348
11.10 Summary 351
Heat Integration Software 351
References 352
Exercises 352
11S-1 Supplements to Chapter 11-MILP and MINLP Applications in HEN Synthesis (Online [...]
11S-1.0 Objectives
11S-1.1 MER Targeting Using Linear Programming (LP)
11S-1.2 MER Design Using Mixed-Integer Linear Programming (MINLP)
11S-1.3 Superstructures for Minimization of Annual Costs
11S-1.4 Case Studies
Case Study 11S-1.1 Optimal Heat-Integration for the ABCDE Process
Case Study 11S-1.2 Optimal Heat-Integration for an Ethylene Plant
11S-1.5 Summary
11S-1.6 References
11S-2 Supplement to Chapter 11-Mass Integration (Online [...]
11S-2.0 Objectives
11S-2.1 Introduction
11S-2.2 Minimum Mass-Separating Agent
11S-2.3 Mass Exchange Networks for Minimum External Area
11S-2.4 Minimum Number of Mass Exchangers
11S-2.5 Advanced Topics
11S-2.6 Summary
11S-2.7 References
Chapter 12 Heat Exchanger Design 358
12.0 Objectives 358
12.1 Introduction 358
12.2 Equipment for Heat Exchange 363
12.3 Heat-Transfer Coefficients and Pressure Drop 375
12.4 Design of Shell-and-Tube Heat Exchangers 380
12.5 Summary 384
References 384
Exercises 384
Chapter 13 Separation Tower Design 386
13.0 Objectives 386
13.1 Operating Conditions 386
13.2 Fenske-Underwood-Gilliland (FUG) Shortcut Method for Ordinary Distillation 387
13.3 Kremser Shortcut Method for Absorption and Stripping 388
13.4 Rigorous Multicomponent, Multiequilibrium-Stage Methods with a Simulator 389
13.5 Plate Efficiency and HETP 391
13.6 Tower Diameter 392
13.7 Pressure Drop and Weeping 393
13.8 Summary 395
References 395
Exercises 396
Chapter 14 Pumps, Compressors, and Expanders 397
14.0 Objectives 397
14.1 Pumps 397
14.2 Compressors and Expanders 401
14.3 Summary 403
References 404
Exercises 404
Chapter 15 Chemical Reactor Design 405
15.0 Objectives 405
15.1 Introduction 405
15.2 Limiting Approximate Models for Tubular Reactors 405
15.3 The COMSOL CFD Package 407
15.4 CFD for Tubular Reactor Models 410
15.5 Nonisothermal Tubular Reactor Models 418
15.6 Mixing in Stirred-Tank Reactors 423
15.7 Summary 424
References 425
Exercises 425
Chapter 16 Cost Accounting and Capital Cost Estimation 426
16.0 Objectives 426
16.1 Accounting 426
16.2 Cost Indexes and Capital Investment 434
16.3 Capital Investment Costs 438
16.4 Estimation of the Total Capital Investment 444
16.5 Purchase Costs of the Most Widely Used Process Equipment 449
16.6 Purchase Costs of Other Chemical Processing Equipment 470
16.7 Equipment Costing Spreadsheet 486
16.8 Equipment Sizing and Capital Cost Estimation Using Aspen Process Economic Analyzer (APEA) 486
16.9 Summary 493
References 493
Exercises 494
Chapter 17 Annual Costs, Earnings, and Profitability Analysis 498
17.0 Objectives 498
17.1 Introduction 498
17.2 Annual Sales Revenues, Production Costs, and the Cost Sheet 499
17.3 Working Capital and Total Capital Investment 509
17.4 Approximate Profitability Measures 510
17.5 Time Value of Money 513
17.6 Cash Flow and Depreciation 520
17.7 Rigorous Profitability Measures 525
17.8 Profitability Analysis Spreadsheet 529
17.9 Summary 545
References 546
Exercises 546
PART THREE DESIGN ANALYSIS-PRODUCT AND PROCESS 551
Chapter 18 Six-Sigma Design Strategies 553
18.0 Objectives 553
18.1 Introduction 553
18.2 Six-Sigma Methodology in Product Design and Manufacturing 553
18.3 Example Applications 557
18.4 Summary 564
References 564
Exercises 565
18S Supplement to Chapter 18 (Online [...]
18S.1 Penicillin Fermenter Model
18S.2 Reactive Extraction and Re-extraction Model
References
Chapter 19 Business Decision Making in Product Development 566
19.0 Objectives 566
19.1 Introduction 566
19.2 Economic Analysis 566
19.3...
| Erscheinungsjahr: | 2019 |
|---|---|
| Genre: | Chemie, Importe |
| Rubrik: | Naturwissenschaften & Technik |
| Medium: | Taschenbuch |
| Inhalt: | Kartoniert / Broschiert |
| ISBN-13: | 9781119588009 |
| ISBN-10: | 1119588006 |
| Sprache: | Englisch |
| Einband: | Kartoniert / Broschiert |
| Autor: |
Lewin, Daniel R.
Seader, J. D. Ng, Ka Ming Gani, Rafiqul Widagdo, Soemantri Seider, Warren D. |
| Hersteller: | John Wiley & Sons Inc |
| Verantwortliche Person für die EU: | Produktsicherheitsverantwortliche/r, Europaallee 1, D-36244 Bad Hersfeld, gpsr@libri.de |
| Maße: | 222 x 279 x 48 mm |
| Von/Mit: | Daniel R. Lewin (u. a.) |
| Erscheinungsdatum: | 17.05.2019 |
| Gewicht: | 1,876 kg |
Warren D. Seider is Professor of Chemical Engineering at the University of Pennsylvania. He received a B.S. degree from the Polytechnic Institute of Brooklyn and M.S. and Ph.D. degrees from the University of Michigan. Seider has contributed to the fields of process analysis, simulation, design, and control. He has authored or coauthored over 110 journal articles and authored or edited seven books. He helped to organize the CACHE (Computer Aids for Chemical Engineering Education) Committee in 1969 and served as its chairman. Seider is a member of the Editorial Advisory Board of Computers and Chemical Engineering.
Daniel R. Lewin is Professor of Chemical Engineering, the Churchill Family Chair, and the Director of the Process Systems Engineering (PSE) research group at the Technion, the Israel Institute of Technology. He received his [...]. from the University of Edinburgh and his [...]. from the Technion. He has authored or co-authored over 100 technical publications in the area of process systems engineering, as well as the first three editions of this textbook, and the multimedia CD that accompanies it.
J. D. Seader is Professor Emeritus of Chemical Engineering at the University of Utah. He received B.S. and M.S. degrees from the University of California at Berkeley and a Ph.D. from the University of Wisconsin. In 2004, he received, with Professor Warren D. Seider, the Warren K. Lewis Award for Chemical Engineering Education from the AIChE. In 2008, his textbook, "Separation Process Principles" with co-author Ernest J. Henley, was cited as one of 30 ground-breaking books in the last 100 years of chemical engineering.
Soemantri Widagdo is a retired R&D executive after a 15-year career at 3M. His last position was the R&D Head of 3M Southeast Asia. He received his B.S. degree in chemical engineering from Bandung Institute of Technology, Indonesia, and his [...].E. and Ph.D. degrees from Stevens Institute of Technology. He has been involved in a variety of technology and product-development programs involving renewable energy, industrial and transportation applications, consumer office products, electrical and electronics applications, health care and dentistry, and display and graphics applications. He has authored and co-authored over 20 technical publications and two patents.
Rafiqul Gani is Professor of System Design at the Department of Chemical & Biochemical Engineering, The Technical University of Denmark and the head and co-founder of the Computer Aided Product-Process Engineering Center (CAPEC). He received a B.S degree from the Bangladesh University of Engineering and Technology, and M.S., DIC and Ph.D. degrees from Imperial College, London. He has published more than 200 peer-reviewed journal articles and delivered over 300 lectures, seminars and plenary/keynote lectures at international conferences, institutions and companies all over the world. Professor Gani is currently (2014-2016) the president of the EFCE (European Federation of Chemical Engineering); a member of the Board of Trustees of the AIChE; a Fellow of the AIChE and also a Fellow of IChemE.
Ka Ming Ng is Chair Professor of Chemical and Biomolecular Engineering at the Hong Kong University of Science and Technology. He obtained his B.S. degree from the University of Minnesota and his Ph.D. from the University of Houston. His research interests center on product conceptualization, process design and business development involving water, natural herbs, nanomaterials, and advanced materials. He is a fellow of the American Institute of Chemical Engineers where he received the Excellence in Process Development Research Award in 2002.
PART ONE INTRODUCTION TO PRODUCT AND PROCESS DESIGN 1
Chapter 1 Introduction to Chemical Product Design 3
1.0 Objectives 3
1.1 Introduction 3
1.2 The Diversity of Chemical Products 3
1.3 Product Design and Development 7
1.4 Summary 16
References 17
Exercises 17
Chapter 2 Introduction to Process Design 19
2.0 Objectives 19
2.1 Introduction 19
2.2 Experiments 21
2.3 Preliminary Process Synthesis 21
2.4 Next Process Design Tasks 40
2.5 Preliminary Flowsheet Mass Balances 41
2.6 Summary 45
References 45
Exercises 45
Chapter 3 Design Literature, Stimulating Innovation, Energy, Environment, Sustainability, Safety, Engineering Ethics 47
3.0 Objectives 47
3.1 Design Literature 47
3.2 Stimulating Invention and Innovation 50
3.3 Energy Sources 51
3.4 Environmental Protection 56
3.5 Sustainability 60
3.6 Safety Considerations 63
3.7 Engineering Ethics 70
3.8 Summary 73
References 73
Exercises 74
3S Supplement to Chapter 3-NSPE Code of Ethics (Online [...]
PART TWO DESIGN SYNTHESIS-PRODUCT AND PROCESSES 77
Chapter 4 Molecular and Mixture Design 79
4.0 Objectives 79
4.1 Introduction 79
4.2 Framework for Computer-Aided Molecular-Mixture Design 81
4.3 Case Studies 98
4.4 Summary 107
References 107
Exercises 108
Chapter 5 Design of Chemical Devices, Functional Products, and Formulated Products 110
5.0 Objectives 110
5.1 Introduction 110
5.2 Design of Chemical Devices and Functional Products 112
5.3 Design of Formulated Products 117
5.4 Design of Processes for B2C Products 123
5.5 Summary 126
References 127
Exercises 127
Chapter 6 Heuristics for Process Synthesis 132
6.0 Objectives 132
6.1 Introduction 133
6.2 Raw Materials and Chemical Reactions 133
6.3 Distribution of Chemicals 135
6.4 Separations 141
6.5 Heat Removal From and Addition to Reactors 145
6.6 Heat Exchangers and Furnaces 148
6.7 Pumping, Compression, Pressure Reduction, Vacuum, and Conveying of Solids 150
6.8 Changing the Particle Size of Solids and Size Separation of Particles 153
6.9 Removal of Particles From Gases and Liquids 154
6.10 Considerations that Apply to the Entire Flowsheet 154
6.11 Summary 155
References 159
Exercises 160
Chapter 7 Simulation to Assist in Process Creation 162
7.0 Objectives 162
7.1 Introduction 162
7.2 Principles of Process Simulation 163
7.3 Process Creation through Process Simulation 176
7.4 Case Studies 184
7.5 Principles of Batch Flowsheet Simulation 194
7.6 Summary 201
References 202
Exercises 202
Chapter 8 Synthesis of Networks Containing Reactors 209
8.0 Objectives 209
8.1 Introduction 209
8.2 Reactor Models in the Process Simulators 210
8.3 Reactor Network Design Using the Attainable Region 215
8.4 Reactor Design for Complex Configurations 220
8.5 Locating the Separation Section with Respect to the Reactor Section 224
8.6 Trade-Offs in Processes Involving Recycle 227
8.7 Optimal Reactor Conversion 228
8.8 Recycle to Extinction 229
8.9 Snowball Effects in the Control of Processes Involving Recycle 231
8.10 Summary 231
References 232
Exercises 232
Chapter 9 Synthesis of Separation Trains 234
9.0 Objectives 234
9.1 Introduction 234
9.2 Criteria for Selection of Separation Methods 241
9.3 Selection of Equipment 244
9.4 Sequencing of Ordinary Distillation Columns for the Separation of Nearly Ideal Liquid Mixtures 245
9.5 Sequencing of Operations for the Separation of Nonideal Liquid Mixtures 257
9.6 Separation Systems for Gas Mixtures 277
9.7 Separation Systems for Solid-Fluid Mixtures 279
9.8 Summary 280
References 280
Exercises 282
Chapter 10 Second-Law Analysis 287
10.0 Objectives 287
10.1 Introduction 287
10.2 The System and the Surroundings 289
10.3 Energy Transfer 289
10.4 Thermodynamic Properties 290
10.5 Equations for Second-Law Analysis 295
10.6 Examples of Lost-Work Calculations 297
10.7 Thermodynamic Efficiency 299
10.8 Causes of Lost Work 300
10.9 Three Examples of Second-Law Analysis 300
10.10 Summary 310
References 310
Exercises 310
Chapter 11 Heat and Power Integration 316
11.0 Objectives 316
11.1 Introduction 316
11.2 Minimum Utility Targets 319
11.3 Networks for Maximum Energy Recovery 325
11.4 Minimum Number of Heat Exchangers 329
11.5 Threshold Approach Temperature 334
11.6 Optimum Approach Temperature 336
11.7 Multiple Utilities 337
11.8 Heat-Integrated Reactors and Distillation Trains 342
11.9 Heat Engines and Heat Pumps 348
11.10 Summary 351
Heat Integration Software 351
References 352
Exercises 352
11S-1 Supplements to Chapter 11-MILP and MINLP Applications in HEN Synthesis (Online [...]
11S-1.0 Objectives
11S-1.1 MER Targeting Using Linear Programming (LP)
11S-1.2 MER Design Using Mixed-Integer Linear Programming (MINLP)
11S-1.3 Superstructures for Minimization of Annual Costs
11S-1.4 Case Studies
Case Study 11S-1.1 Optimal Heat-Integration for the ABCDE Process
Case Study 11S-1.2 Optimal Heat-Integration for an Ethylene Plant
11S-1.5 Summary
11S-1.6 References
11S-2 Supplement to Chapter 11-Mass Integration (Online [...]
11S-2.0 Objectives
11S-2.1 Introduction
11S-2.2 Minimum Mass-Separating Agent
11S-2.3 Mass Exchange Networks for Minimum External Area
11S-2.4 Minimum Number of Mass Exchangers
11S-2.5 Advanced Topics
11S-2.6 Summary
11S-2.7 References
Chapter 12 Heat Exchanger Design 358
12.0 Objectives 358
12.1 Introduction 358
12.2 Equipment for Heat Exchange 363
12.3 Heat-Transfer Coefficients and Pressure Drop 375
12.4 Design of Shell-and-Tube Heat Exchangers 380
12.5 Summary 384
References 384
Exercises 384
Chapter 13 Separation Tower Design 386
13.0 Objectives 386
13.1 Operating Conditions 386
13.2 Fenske-Underwood-Gilliland (FUG) Shortcut Method for Ordinary Distillation 387
13.3 Kremser Shortcut Method for Absorption and Stripping 388
13.4 Rigorous Multicomponent, Multiequilibrium-Stage Methods with a Simulator 389
13.5 Plate Efficiency and HETP 391
13.6 Tower Diameter 392
13.7 Pressure Drop and Weeping 393
13.8 Summary 395
References 395
Exercises 396
Chapter 14 Pumps, Compressors, and Expanders 397
14.0 Objectives 397
14.1 Pumps 397
14.2 Compressors and Expanders 401
14.3 Summary 403
References 404
Exercises 404
Chapter 15 Chemical Reactor Design 405
15.0 Objectives 405
15.1 Introduction 405
15.2 Limiting Approximate Models for Tubular Reactors 405
15.3 The COMSOL CFD Package 407
15.4 CFD for Tubular Reactor Models 410
15.5 Nonisothermal Tubular Reactor Models 418
15.6 Mixing in Stirred-Tank Reactors 423
15.7 Summary 424
References 425
Exercises 425
Chapter 16 Cost Accounting and Capital Cost Estimation 426
16.0 Objectives 426
16.1 Accounting 426
16.2 Cost Indexes and Capital Investment 434
16.3 Capital Investment Costs 438
16.4 Estimation of the Total Capital Investment 444
16.5 Purchase Costs of the Most Widely Used Process Equipment 449
16.6 Purchase Costs of Other Chemical Processing Equipment 470
16.7 Equipment Costing Spreadsheet 486
16.8 Equipment Sizing and Capital Cost Estimation Using Aspen Process Economic Analyzer (APEA) 486
16.9 Summary 493
References 493
Exercises 494
Chapter 17 Annual Costs, Earnings, and Profitability Analysis 498
17.0 Objectives 498
17.1 Introduction 498
17.2 Annual Sales Revenues, Production Costs, and the Cost Sheet 499
17.3 Working Capital and Total Capital Investment 509
17.4 Approximate Profitability Measures 510
17.5 Time Value of Money 513
17.6 Cash Flow and Depreciation 520
17.7 Rigorous Profitability Measures 525
17.8 Profitability Analysis Spreadsheet 529
17.9 Summary 545
References 546
Exercises 546
PART THREE DESIGN ANALYSIS-PRODUCT AND PROCESS 551
Chapter 18 Six-Sigma Design Strategies 553
18.0 Objectives 553
18.1 Introduction 553
18.2 Six-Sigma Methodology in Product Design and Manufacturing 553
18.3 Example Applications 557
18.4 Summary 564
References 564
Exercises 565
18S Supplement to Chapter 18 (Online [...]
18S.1 Penicillin Fermenter Model
18S.2 Reactive Extraction and Re-extraction Model
References
Chapter 19 Business Decision Making in Product Development 566
19.0 Objectives 566
19.1 Introduction 566
19.2 Economic Analysis 566
19.3...
| Erscheinungsjahr: | 2019 |
|---|---|
| Genre: | Chemie, Importe |
| Rubrik: | Naturwissenschaften & Technik |
| Medium: | Taschenbuch |
| Inhalt: | Kartoniert / Broschiert |
| ISBN-13: | 9781119588009 |
| ISBN-10: | 1119588006 |
| Sprache: | Englisch |
| Einband: | Kartoniert / Broschiert |
| Autor: |
Lewin, Daniel R.
Seader, J. D. Ng, Ka Ming Gani, Rafiqul Widagdo, Soemantri Seider, Warren D. |
| Hersteller: | John Wiley & Sons Inc |
| Verantwortliche Person für die EU: | Produktsicherheitsverantwortliche/r, Europaallee 1, D-36244 Bad Hersfeld, gpsr@libri.de |
| Maße: | 222 x 279 x 48 mm |
| Von/Mit: | Daniel R. Lewin (u. a.) |
| Erscheinungsdatum: | 17.05.2019 |
| Gewicht: | 1,876 kg |
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