{"product_id":"product-and-process-design-principles-isbn-9781119282631","title":"Product and Process Design Principles","description":"The new 4\u003csup\u003eth\u003c\/sup\u003e edition of Seider’s \u003cb\u003e\u003ci\u003eProduct and Process Design Principles: Synthesis, Analysis and Design\u003c\/i\u003e\u003c\/b\u003e 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. \u003cp\u003e\u003cb\u003ePART ONE INTRODUCTION TO PRODUCT AND PROCESS DESIGN 1\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e1 \u003c\/b\u003e\u003cb\u003eIntroduction to Chemical Product Design 3\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e1.0 Objectives 3\u003c\/p\u003e \u003cp\u003e1.1 Introduction 3\u003c\/p\u003e \u003cp\u003e1.2 The Diversity of Chemical Products 3\u003c\/p\u003e \u003cp\u003e1.3 Product Design and Development 7\u003c\/p\u003e \u003cp\u003e1.4 Summary 16\u003c\/p\u003e \u003cp\u003eReferences 17\u003c\/p\u003e \u003cp\u003eExercises 17\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e2 \u003c\/b\u003e\u003cb\u003eIntroduction to Process Design 19\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e2.0 Objectives 19\u003c\/p\u003e \u003cp\u003e2.1 Introduction 19\u003c\/p\u003e \u003cp\u003e2.2 Experiments 21\u003c\/p\u003e \u003cp\u003e2.3 Preliminary Process Synthesis 21\u003c\/p\u003e \u003cp\u003e2.4 Next Process Design Tasks 40\u003c\/p\u003e \u003cp\u003e2.5 Preliminary Flowsheet Mass Balances 41\u003c\/p\u003e \u003cp\u003e2.6 Summary 45\u003c\/p\u003e \u003cp\u003eReferences 45\u003c\/p\u003e \u003cp\u003eExercises 45\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e3 \u003c\/b\u003e\u003cb\u003eDesign Literature, Stimulating Innovation, Energy, Environment, Sustainability, Safety, Engineering Ethics 47\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e3.0 Objectives 47\u003c\/p\u003e \u003cp\u003e3.1 Design Literature 47\u003c\/p\u003e \u003cp\u003e3.2 Stimulating Invention and Innovation 50\u003c\/p\u003e \u003cp\u003e3.3 Energy Sources 51\u003c\/p\u003e \u003cp\u003e3.4 Environmental Protection 56\u003c\/p\u003e \u003cp\u003e3.5 Sustainability 60\u003c\/p\u003e \u003cp\u003e3.6 Safety Considerations 63\u003c\/p\u003e \u003cp\u003e3.7 Engineering Ethics 70\u003c\/p\u003e \u003cp\u003e3.8 Summary 73\u003c\/p\u003e \u003cp\u003eReferences 73\u003c\/p\u003e \u003cp\u003eExercises 74\u003c\/p\u003e \u003cp\u003e3S Supplement to Chapter 3—NSPE Code of Ethics (Online www.wiley.com\/college\/Seider)\u003c\/p\u003e \u003cp\u003e\u003cb\u003ePART TWO DESIGN SYNTHESIS—PRODUCT AND PROCESSES 77\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter 4 \u003c\/b\u003e\u003cb\u003eMolecular and Mixture Design 79\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e4.0 Objectives 79\u003c\/p\u003e \u003cp\u003e4.1 Introduction 79\u003c\/p\u003e \u003cp\u003e4.2 Framework for Computer-Aided Molecular-Mixture Design 81\u003c\/p\u003e \u003cp\u003e4.3 Case Studies 98\u003c\/p\u003e \u003cp\u003e4.4 Summary 107\u003c\/p\u003e \u003cp\u003eReferences 107\u003c\/p\u003e \u003cp\u003eExercises 108\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e5 \u003c\/b\u003e\u003cb\u003eDesign of Chemical Devices, Functional Products, and Formulated Products 110\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e5.0 Objectives 110\u003c\/p\u003e \u003cp\u003e5.1 Introduction 110\u003c\/p\u003e \u003cp\u003e5.2 Design of Chemical Devices and Functional Products 112\u003c\/p\u003e \u003cp\u003e5.3 Design of Formulated Products 117\u003c\/p\u003e \u003cp\u003e5.4 Design of Processes for B2C Products 123\u003c\/p\u003e \u003cp\u003e5.5 Summary 126\u003c\/p\u003e \u003cp\u003eReferences 127\u003c\/p\u003e \u003cp\u003eExercises 127\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e6 \u003c\/b\u003e\u003cb\u003eHeuristics for Process Synthesis 132\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e6.0 Objectives 132\u003c\/p\u003e \u003cp\u003e6.1 Introduction 133\u003c\/p\u003e \u003cp\u003e6.2 Raw Materials and Chemical Reactions 133\u003c\/p\u003e \u003cp\u003e6.3 Distribution of Chemicals 135\u003c\/p\u003e \u003cp\u003e6.4 Separations 141\u003c\/p\u003e \u003cp\u003e6.5 Heat Removal From and Addition to Reactors 145\u003c\/p\u003e \u003cp\u003e6.6 Heat Exchangers and Furnaces 148\u003c\/p\u003e \u003cp\u003e6.7 Pumping, Compression, Pressure Reduction, Vacuum, and Conveying of Solids 150\u003c\/p\u003e \u003cp\u003e6.8 Changing the Particle Size of Solids and Size Separation of Particles 153\u003c\/p\u003e \u003cp\u003e6.9 Removal of Particles From Gases and Liquids 154\u003c\/p\u003e \u003cp\u003e6.10 Considerations that Apply to the Entire Flowsheet 154\u003c\/p\u003e \u003cp\u003e6.11 Summary 155\u003c\/p\u003e \u003cp\u003eReferences 159\u003c\/p\u003e \u003cp\u003eExercises 160\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e7 \u003c\/b\u003e\u003cb\u003eSimulation to Assist in Process Creation 162\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e7.0 Objectives 162\u003c\/p\u003e \u003cp\u003e7.1 Introduction 162\u003c\/p\u003e \u003cp\u003e7.2 Principles of Process Simulation 163\u003c\/p\u003e \u003cp\u003e7.3 Process Creation through Process Simulation 176\u003c\/p\u003e \u003cp\u003e7.4 Case Studies 184\u003c\/p\u003e \u003cp\u003e7.5 Principles of Batch Flowsheet Simulation 194\u003c\/p\u003e \u003cp\u003e7.6 Summary 201\u003c\/p\u003e \u003cp\u003eReferences 202\u003c\/p\u003e \u003cp\u003eExercises 202\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e8 \u003c\/b\u003e\u003cb\u003eSynthesis of Networks Containing Reactors 209\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e8.0 Objectives 209\u003c\/p\u003e \u003cp\u003e8.1 Introduction 209\u003c\/p\u003e \u003cp\u003e8.2 Reactor Models in the Process Simulators 210\u003c\/p\u003e \u003cp\u003e8.3 Reactor Network Design Using the Attainable Region 215\u003c\/p\u003e \u003cp\u003e8.4 Reactor Design for Complex Configurations 220\u003c\/p\u003e \u003cp\u003e8.5 Locating the Separation Section with Respect to the Reactor Section 224\u003c\/p\u003e \u003cp\u003e8.6 Trade-Offs in Processes Involving Recycle 227\u003c\/p\u003e \u003cp\u003e8.7 Optimal Reactor Conversion 228\u003c\/p\u003e \u003cp\u003e8.8 Recycle to Extinction 229\u003c\/p\u003e \u003cp\u003e8.9 Snowball Effects in the Control of Processes Involving Recycle 231\u003c\/p\u003e \u003cp\u003e8.10 Summary 231\u003c\/p\u003e \u003cp\u003eReferences 232\u003c\/p\u003e \u003cp\u003eExercises 232\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e9 \u003c\/b\u003e\u003cb\u003eSynthesis of Separation Trains 234\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e9.0 Objectives 234\u003c\/p\u003e \u003cp\u003e9.1 Introduction 234\u003c\/p\u003e \u003cp\u003e9.2 Criteria for Selection of Separation Methods 241\u003c\/p\u003e \u003cp\u003e9.3 Selection of Equipment 244\u003c\/p\u003e \u003cp\u003e9.4 Sequencing of Ordinary Distillation Columns for the Separation of Nearly Ideal Liquid Mixtures 245\u003c\/p\u003e \u003cp\u003e9.5 Sequencing of Operations for the Separation of Nonideal Liquid Mixtures 257\u003c\/p\u003e \u003cp\u003e9.6 Separation Systems for Gas Mixtures 277\u003c\/p\u003e \u003cp\u003e9.7 Separation Systems for Solid-Fluid Mixtures 279\u003c\/p\u003e \u003cp\u003e9.8 Summary 280\u003c\/p\u003e \u003cp\u003eReferences 280\u003c\/p\u003e \u003cp\u003eExercises 282\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e10 \u003c\/b\u003e\u003cb\u003eSecond-Law Analysis 287\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e10.0 Objectives 287\u003c\/p\u003e \u003cp\u003e10.1 Introduction 287\u003c\/p\u003e \u003cp\u003e10.2 The System and the Surroundings 289\u003c\/p\u003e \u003cp\u003e10.3 Energy Transfer 289\u003c\/p\u003e \u003cp\u003e10.4 Thermodynamic Properties 290\u003c\/p\u003e \u003cp\u003e10.5 Equations for Second-Law Analysis 295\u003c\/p\u003e \u003cp\u003e10.6 Examples of Lost-Work Calculations 297\u003c\/p\u003e \u003cp\u003e10.7 Thermodynamic Efficiency 299\u003c\/p\u003e \u003cp\u003e10.8 Causes of Lost Work 300\u003c\/p\u003e \u003cp\u003e10.9 Three Examples of Second-Law Analysis 300\u003c\/p\u003e \u003cp\u003e10.10 Summary 310\u003c\/p\u003e \u003cp\u003eReferences 310\u003c\/p\u003e \u003cp\u003eExercises 310\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e11 \u003c\/b\u003e\u003cb\u003eHeat and Power Integration 316\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e11.0 Objectives 316\u003c\/p\u003e \u003cp\u003e11.1 Introduction 316\u003c\/p\u003e \u003cp\u003e11.2 Minimum Utility Targets 319\u003c\/p\u003e \u003cp\u003e11.3 Networks for Maximum Energy Recovery 325\u003c\/p\u003e \u003cp\u003e11.4 Minimum Number of Heat Exchangers 329\u003c\/p\u003e \u003cp\u003e11.5 Threshold Approach Temperature 334\u003c\/p\u003e \u003cp\u003e11.6 Optimum Approach Temperature 336\u003c\/p\u003e \u003cp\u003e11.7 Multiple Utilities 337\u003c\/p\u003e \u003cp\u003e11.8 Heat-Integrated Reactors and Distillation Trains 342\u003c\/p\u003e \u003cp\u003e11.9 Heat Engines and Heat Pumps 348\u003c\/p\u003e \u003cp\u003e11.10 Summary 351\u003c\/p\u003e \u003cp\u003eHeat Integration Software 351\u003c\/p\u003e \u003cp\u003eReferences 352\u003c\/p\u003e \u003cp\u003eExercises 352\u003c\/p\u003e \u003cp\u003e11S-1 Supplements to Chapter 11—MILP and MINLP Applications in HEN Synthesis (Online www.wiley.com\/college\/Seider)\u003c\/p\u003e \u003cp\u003e11S-1.0 Objectives\u003c\/p\u003e \u003cp\u003e11S-1.1 MER Targeting Using Linear Programming (LP)\u003c\/p\u003e \u003cp\u003e11S-1.2 MER Design Using Mixed-Integer Linear Programming (MINLP)\u003c\/p\u003e \u003cp\u003e11S-1.3 Superstructures for Minimization of Annual Costs\u003c\/p\u003e \u003cp\u003e11S-1.4 Case Studies\u003c\/p\u003e \u003cp\u003eCase Study 11S-1.1 Optimal Heat-Integration for the ABCDE Process\u003c\/p\u003e \u003cp\u003eCase Study 11S-1.2 Optimal Heat-Integration for an Ethylene Plant\u003c\/p\u003e \u003cp\u003e11S-1.5 Summary\u003c\/p\u003e \u003cp\u003e11S-1.6 References\u003c\/p\u003e \u003cp\u003e11S-2 Supplement to Chapter 11—Mass Integration (Online www.wiley.com\/college\/Seider)\u003c\/p\u003e \u003cp\u003e11S-2.0 Objectives\u003c\/p\u003e \u003cp\u003e11S-2.1 Introduction\u003c\/p\u003e \u003cp\u003e11S-2.2 Minimum Mass-Separating Agent\u003c\/p\u003e \u003cp\u003e11S-2.3 Mass Exchange Networks for Minimum External Area\u003c\/p\u003e \u003cp\u003e11S-2.4 Minimum Number of Mass Exchangers\u003c\/p\u003e \u003cp\u003e11S-2.5 Advanced Topics\u003c\/p\u003e \u003cp\u003e11S-2.6 Summary\u003c\/p\u003e \u003cp\u003e11S-2.7 References\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e12 \u003c\/b\u003e\u003cb\u003eHeat Exchanger Design 358\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e12.0 Objectives 358\u003c\/p\u003e \u003cp\u003e12.1 Introduction 358\u003c\/p\u003e \u003cp\u003e12.2 Equipment for Heat Exchange 363\u003c\/p\u003e \u003cp\u003e12.3 Heat-Transfer Coefficients and Pressure Drop 375\u003c\/p\u003e \u003cp\u003e12.4 Design of Shell-and-Tube Heat Exchangers 380\u003c\/p\u003e \u003cp\u003e12.5 Summary 384\u003c\/p\u003e \u003cp\u003eReferences 384\u003c\/p\u003e \u003cp\u003eExercises 384\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e13 \u003c\/b\u003e\u003cb\u003eSeparation Tower Design 386\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e13.0 Objectives 386\u003c\/p\u003e \u003cp\u003e13.1 Operating Conditions 386\u003c\/p\u003e \u003cp\u003e13.2 Fenske-Underwood-Gilliland (FUG) Shortcut Method for Ordinary Distillation 387\u003c\/p\u003e \u003cp\u003e13.3 Kremser Shortcut Method for Absorption and Stripping 388\u003c\/p\u003e \u003cp\u003e13.4 Rigorous Multicomponent, Multiequilibrium-Stage Methods with a Simulator 389\u003c\/p\u003e \u003cp\u003e13.5 Plate Efficiency and HETP 391\u003c\/p\u003e \u003cp\u003e13.6 Tower Diameter 392\u003c\/p\u003e \u003cp\u003e13.7 Pressure Drop and Weeping 393\u003c\/p\u003e \u003cp\u003e13.8 Summary 395\u003c\/p\u003e \u003cp\u003eReferences 395\u003c\/p\u003e \u003cp\u003eExercises 396\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e14 \u003c\/b\u003e\u003cb\u003ePumps, Compressors, and Expanders 397\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e14.0 Objectives 397\u003c\/p\u003e \u003cp\u003e14.1 Pumps 397\u003c\/p\u003e \u003cp\u003e14.2 Compressors and Expanders 401\u003c\/p\u003e \u003cp\u003e14.3 Summary 403\u003c\/p\u003e \u003cp\u003eReferences 404\u003c\/p\u003e \u003cp\u003eExercises 404\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e15 \u003c\/b\u003e\u003cb\u003eChemical Reactor Design 405\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e15.0 Objectives 405\u003c\/p\u003e \u003cp\u003e15.1 Introduction 405\u003c\/p\u003e \u003cp\u003e15.2 Limiting Approximate Models for Tubular Reactors 405\u003c\/p\u003e \u003cp\u003e15.3 The COMSOL CFD Package 407\u003c\/p\u003e \u003cp\u003e15.4 CFD for Tubular Reactor Models 410\u003c\/p\u003e \u003cp\u003e15.5 Nonisothermal Tubular Reactor Models 418\u003c\/p\u003e \u003cp\u003e15.6 Mixing in Stirred-Tank Reactors 423\u003c\/p\u003e \u003cp\u003e15.7 Summary 424\u003c\/p\u003e \u003cp\u003eReferences 425\u003c\/p\u003e \u003cp\u003eExercises 425\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e16 \u003c\/b\u003e\u003cb\u003eCost Accounting and Capital Cost Estimation 426\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e16.0 Objectives 426\u003c\/p\u003e \u003cp\u003e16.1 Accounting 426\u003c\/p\u003e \u003cp\u003e16.2 Cost Indexes and Capital Investment 434\u003c\/p\u003e \u003cp\u003e16.3 Capital Investment Costs 438\u003c\/p\u003e \u003cp\u003e16.4 Estimation of the Total Capital Investment 444\u003c\/p\u003e \u003cp\u003e16.5 Purchase Costs of the Most Widely Used Process Equipment 449\u003c\/p\u003e \u003cp\u003e16.6 Purchase Costs of Other Chemical Processing Equipment 470\u003c\/p\u003e \u003cp\u003e16.7 Equipment Costing Spreadsheet 486\u003c\/p\u003e \u003cp\u003e16.8 Equipment Sizing and Capital Cost Estimation Using Aspen Process Economic Analyzer (APEA) 486\u003c\/p\u003e \u003cp\u003e16.9 Summary 493\u003c\/p\u003e \u003cp\u003eReferences 493\u003c\/p\u003e \u003cp\u003eExercises 494\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e17 \u003c\/b\u003e\u003cb\u003eAnnual Costs, Earnings, and Profitability Analysis 498\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e17.0 Objectives 498\u003c\/p\u003e \u003cp\u003e17.1 Introduction 498\u003c\/p\u003e \u003cp\u003e17.2 Annual Sales Revenues, Production Costs, and the Cost Sheet 499\u003c\/p\u003e \u003cp\u003e17.3 Working Capital and Total Capital Investment 509\u003c\/p\u003e \u003cp\u003e17.4 Approximate Profitability Measures 510\u003c\/p\u003e \u003cp\u003e17.5 Time Value of Money 513\u003c\/p\u003e \u003cp\u003e17.6 Cash Flow and Depreciation 520\u003c\/p\u003e \u003cp\u003e17.7 Rigorous Profitability Measures 525\u003c\/p\u003e \u003cp\u003e17.8 Profitability Analysis Spreadsheet 529\u003c\/p\u003e \u003cp\u003e17.9 Summary 545\u003c\/p\u003e \u003cp\u003eReferences 546\u003c\/p\u003e \u003cp\u003eExercises 546\u003c\/p\u003e \u003cp\u003e\u003cb\u003ePART THREE DESIGN ANALYSIS—PRODUCT AND PROCESS 551\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e18 \u003c\/b\u003e\u003cb\u003eSix-Sigma Design Strategies 553\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e18.0 Objectives 553\u003c\/p\u003e \u003cp\u003e18.1 Introduction 553\u003c\/p\u003e \u003cp\u003e18.2 Six-Sigma Methodology in Product Design and Manufacturing 553\u003c\/p\u003e \u003cp\u003e18.3 Example Applications 557\u003c\/p\u003e \u003cp\u003e18.4 Summary 564\u003c\/p\u003e \u003cp\u003eReferences 564\u003c\/p\u003e \u003cp\u003eExercises 565\u003c\/p\u003e \u003cp\u003e18S Supplement to Chapter 18 (Online www.wiley.com\/college\/Seider)\u003c\/p\u003e \u003cp\u003e18S.1 Penicillin Fermenter Model\u003c\/p\u003e \u003cp\u003e18S.2 Reactive Extraction and Re-extraction Model\u003c\/p\u003e \u003cp\u003eReferences\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e19 \u003c\/b\u003e\u003cb\u003eBusiness Decision Making in Product Development 566\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e19.0 Objectives 566\u003c\/p\u003e \u003cp\u003e19.1 Introduction 566\u003c\/p\u003e \u003cp\u003e19.2 Economic Analysis 566\u003c\/p\u003e \u003cp\u003e19.3 Make-or-Buy Decisions 570\u003c\/p\u003e \u003cp\u003e19.4 Microeconomics of Product Development 572\u003c\/p\u003e \u003cp\u003e19.5 Company and Societal Factors Affecting Product Development 573\u003c\/p\u003e \u003cp\u003e19.6 Summary 574\u003c\/p\u003e \u003cp\u003eReferences 575\u003c\/p\u003e \u003cp\u003eExercises 575\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e20 \u003c\/b\u003e\u003cb\u003ePlantwide Controllability Assessment 576\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e20.0 Objectives 576\u003c\/p\u003e \u003cp\u003e20.1 Introduction 576\u003c\/p\u003e \u003cp\u003e20.2 Control System Configuration 579\u003c\/p\u003e \u003cp\u003e20.3 Qualitative Plantwide Control System Synthesis 584\u003c\/p\u003e \u003cp\u003e20.4 Summary 590\u003c\/p\u003e \u003cp\u003eReferences 590\u003c\/p\u003e \u003cp\u003eExercises 591\u003c\/p\u003e \u003cp\u003e20S Supplement to Chapter 20 (Online www.wiley.com\/college\/Seider)\u003c\/p\u003e \u003cp\u003e20S.0 Objectives\u003c\/p\u003e \u003cp\u003e20S.1 Generation of Linear Models in Standard Forms\u003c\/p\u003e \u003cp\u003e20S.2 Quantitative Measures for Controllability and Resiliency\u003c\/p\u003e \u003cp\u003e20S.3 Towards Automated Flowsheet C\u0026amp;R Diagnosis\u003c\/p\u003e \u003cp\u003e20S.4 Control Loop Definition and Tuning\u003c\/p\u003e \u003cp\u003e20S.5 Case Studies\u003c\/p\u003e \u003cp\u003eCase Study 20S.1 Exothermic Reactor Design for the Production of Propylene Glycol\u003c\/p\u003e \u003cp\u003eCase Study 20S.2 Two Alternative Heat Exchanger Networks\u003c\/p\u003e \u003cp\u003eCase Study 20S.3 Interaction of design and Control in the MCB Separation Process\u003c\/p\u003e \u003cp\u003e20S.6 MATLAB for C\u0026amp;R Analysis\u003c\/p\u003e \u003cp\u003e20S.7 Summary\u003c\/p\u003e \u003cp\u003eReferences\u003c\/p\u003e \u003cp\u003eExercises\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e21 \u003c\/b\u003e\u003cb\u003eDesign Optimization 597\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e21.0 Objectives 597\u003c\/p\u003e \u003cp\u003e21.1 Introduction 597\u003c\/p\u003e \u003cp\u003e21.2 General Formulation of the Optimization Problem 598\u003c\/p\u003e \u003cp\u003e21.3 Classification of Optimization Problems 599\u003c\/p\u003e \u003cp\u003e21.4 Linear Programming (LP) 601\u003c\/p\u003e \u003cp\u003e21.5 Nonlinear Programming (NLP) with a Single Variable 603\u003c\/p\u003e \u003cp\u003e21.6 Conditions for Nonlinear Programming (NLP) by Gradient Methods with Two or More Decision Variables 605\u003c\/p\u003e \u003cp\u003e21.7 Optimization Algorithm 607\u003c\/p\u003e \u003cp\u003e21.8 Flowsheet Optimizations—Case Studies 609\u003c\/p\u003e \u003cp\u003e21.9 Summary 611\u003c\/p\u003e \u003cp\u003eReferences 612\u003c\/p\u003e \u003cp\u003eExercises 612\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e22 \u003c\/b\u003e\u003cb\u003eOptimal Design and Scheduling of Batch Processes 616\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e22.0 Objectives 616\u003c\/p\u003e \u003cp\u003e22.1 Introduction 616\u003c\/p\u003e \u003cp\u003e22.2 Design of Batch Process Units 617\u003c\/p\u003e \u003cp\u003e22.3 Design of Reactor–Separator Processes 620\u003c\/p\u003e \u003cp\u003e22.4 Design of Single-product Processing Sequences 622\u003c\/p\u003e \u003cp\u003e22.5 Design on Multiproduct Processing Sequences 625\u003c\/p\u003e \u003cp\u003e22.6 Summary 626\u003c\/p\u003e \u003cp\u003eReferences 626\u003c\/p\u003e \u003cp\u003eExercises 627\u003c\/p\u003e \u003cp\u003e\u003cb\u003ePART FOUR DESIGN REPORTS—PRODUCT AND PROCESS 629\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e23 \u003c\/b\u003e\u003cb\u003eWritten Reports and Oral Presentations 631\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e23.0 Objectives 631\u003c\/p\u003e \u003cp\u003e23.1 Contents of the Written Report 632\u003c\/p\u003e \u003cp\u003e23.2 Preparation of the Written Report 636\u003c\/p\u003e \u003cp\u003e23.3 Oral Design Presentations 638\u003c\/p\u003e \u003cp\u003e23.4 Award Competition 641\u003c\/p\u003e \u003cp\u003e23.5 Summary 641\u003c\/p\u003e \u003cp\u003eReferences 641\u003c\/p\u003e \u003cp\u003e\u003cb\u003ePART FIVE CASE STUDIES—PRODUCT AND PROCESS DESIGNS 643\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e24 \u003c\/b\u003e\u003cb\u003eCase Study 1—Home Hemodialysis Devices 645\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e24.0 Objectives 645\u003c\/p\u003e \u003cp\u003e24.1 Hemodialysis Technology 645\u003c\/p\u003e \u003cp\u003e24.2 Design Specifications of Home Hemodialysis Device 652\u003c\/p\u003e \u003cp\u003e24.3 Summary 655\u003c\/p\u003e \u003cp\u003eReferences 655\u003c\/p\u003e \u003cp\u003eBibliography Patents—Hemodialysis Devices—General 655\u003c\/p\u003e \u003cp\u003ePatents—Hemodialysis Devices—Hollow-Fiber Membranes 656\u003c\/p\u003e \u003cp\u003ePatents—Hemodialysis Devices—Dialysate Regeneration 656\u003c\/p\u003e \u003cp\u003ePatents—Hemodialysis Devices—Alarms\/User Interface 656\u003c\/p\u003e \u003cp\u003eExercises 656\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e25 \u003c\/b\u003e\u003cb\u003eCase Study 2—High Throughput Screening Devices for Kinase \u003c\/b\u003e\u003cb\u003eInhibitors 657\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e25.0 Objectives 657\u003c\/p\u003e \u003cp\u003e25.1 Background Technology For High Throughput Screening of Kinase Inhibitors 657\u003c\/p\u003e \u003cp\u003e25.2 Product Concept 665\u003c\/p\u003e \u003cp\u003e25.3 Prototyping 669\u003c\/p\u003e \u003cp\u003e25.4 Product Development 672\u003c\/p\u003e \u003cp\u003e25.5 Summary 672\u003c\/p\u003e \u003cp\u003eReferences 672\u003c\/p\u003e \u003cp\u003ePatents 673\u003c\/p\u003e \u003cp\u003eExercises 673\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e26 \u003c\/b\u003e\u003cb\u003eCase Study 3—Die Attach Adhesive: A Case Study of Product \u003c\/b\u003e\u003cb\u003eDevelopment 674\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e26.0 Objectives 674\u003c\/p\u003e \u003cp\u003e26.1 Background of Technology 674\u003c\/p\u003e \u003cp\u003e26.2 Market Study 674\u003c\/p\u003e \u003cp\u003e26.3 Product Design 677\u003c\/p\u003e \u003cp\u003e26.4 Process Design 678\u003c\/p\u003e \u003cp\u003e26.5 Prototyping 678\u003c\/p\u003e \u003cp\u003e26.6 Estimation of Product Cost 679\u003c\/p\u003e \u003cp\u003e26.7 Summary 680\u003c\/p\u003e \u003cp\u003eReferences 680\u003c\/p\u003e \u003cp\u003eExercises 681\u003c\/p\u003e \u003cp\u003e\u003cb\u003eChapter \u003c\/b\u003e\u003cb\u003e27 \u003c\/b\u003e\u003cb\u003eCase Study 4—Ammonia Process 683\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003e27.0 Objectives 683\u003c\/p\u003e \u003cp\u003e27.1 Introduction 683\u003c\/p\u003e \u003cp\u003e27.2 Initial Base Case Design 686\u003c\/p\u003e \u003cp\u003e27.3 Design Refinement 692\u003c\/p\u003e \u003cp\u003ePostscript 699\u003c\/p\u003e \u003cp\u003eReferences 703\u003c\/p\u003e \u003cp\u003eExercises 703\u003c\/p\u003e \u003cp\u003e\u003cb\u003eAPPENDICES\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eI. Residue Curves for Heterogeneous Systems 704\u003c\/p\u003e \u003cp\u003eII. Design Problem Statements by Area 705\u003c\/p\u003e \u003cp\u003eIII. Materials of Construction 709\u003c\/p\u003e \u003cp\u003e\u003cb\u003eINDICES\u003c\/b\u003e\u003c\/p\u003e \u003cp\u003eTable of Acronyms 711\u003c\/p\u003e \u003cp\u003eAuthor Index 719\u003c\/p\u003e \u003cp\u003eSubject Index 725\u003c\/p\u003e \u003cp\u003e\u003cb\u003eWarren D. Seider\u003c\/b\u003e 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 \u003ci\u003eComputers and Chemical Engineering\u003c\/i\u003e.\u003c\/p\u003e \u003cp\u003e\u003cb\u003eDaniel R. Lewin\u003c\/b\u003e 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 B.Sc. from the University of Edinburgh and his D.Sc. 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.\u003c\/p\u003e \u003cp\u003e\u003cb\u003eJ. D. Seader\u003c\/b\u003e 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.\u003c\/p\u003e \u003cp\u003e\u003cb\u003eSoemantri Widagdo\u003c\/b\u003e is a retired R\u0026amp;D executive after a 15-year career at 3M. His last position was the R\u0026amp;D Head of 3M Southeast Asia. He received his B.S. degree in chemical engineering from Bandung Institute of Technology, Indonesia, and his M.Ch.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.\u003c\/p\u003e \u003cp\u003e\u003cb\u003eRafiqul Gani\u003c\/b\u003e is Professor of System Design at the Department of Chemical \u0026amp; 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.\u003c\/p\u003e \u003cp\u003e\u003cb\u003eKa Ming Ng\u003c\/b\u003e 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.\u003c\/p\u003e   \u003cp\u003eGet off to a great start with \u003cb\u003eWiley StudentQuickStart.\u003c\/b\u003e  \u003c\/p\u003e\u003cp\u003eGive your students free access to the e-textbook for 14 days and the choice to purchase the format they prefer, all at affordable prices available through \u003cb\u003ewww.wileystudentquickstart.com.\u003c\/b\u003e  \u003c\/p\u003e\u003cp\u003eWiley StudentQuickStart offers students:  \u003c\/p\u003e\u003cul\u003e \u003cli\u003e\n\u003cb\u003eImmediate Access:\u003c\/b\u003e The free 14-day trial of the e-textbook ensures students have the right course materials right away.\u003c\/li\u003e \u003cli\u003e\n\u003cb\u003eChoice:\u003c\/b\u003e Wiley StudentQuickStart offers students the option to rent or purchase an e-textbook, or purchase a print book, all at affordable prices.\u003c\/li\u003e \u003cli\u003e\n\u003cb\u003eA Better User Experience:\u003c\/b\u003e With enhanced e-textbook capabilities, students can search content, highlight, take and share notes, and study anytime, anywhere, and on the device of their choice.\u003c\/li\u003e \u003c\/ul\u003e  \u003cp\u003eHelp your students launch into learning today. Send them to \u003cb\u003ewww.wileystudentquickstart.com\u003c\/b\u003e for a free trial and exceptionally affordable prices. Or contact your Wiley representative to learn more.\u003c\/p\u003e","brand":"Wiley","offers":[{"title":"Default Title","offer_id":47989863645413,"sku":"NP9781119282631","price":110.0,"currency_code":"USD","in_stock":false}],"thumbnail_url":"\/\/cdn.shopify.com\/s\/files\/1\/1842\/7735\/files\/9781119282631.jpg?v=1761785717","url":"https:\/\/k12savings.com\/products\/product-and-process-design-principles-isbn-9781119282631","provider":"K12savings","version":"1.0","type":"link"}