Tuesday, July 19, 2022

Product and Process Design Principles: Synthesis, Analysis and Evaluation - Book Information

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

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


ISBN: 978-1-119-28263-1 May 2016 784 Pages

https://www.wiley.com/en-us/Product+and+Process+Design+Principles%3A+Synthesis%2C+Analysis+and+Evaluation%2C+4th+Edition-p-9781119282631


TABLE OF CONTENTS

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 www.wiley.com/college/Seider)


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 www.wiley.com/college/Seider)


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 www.wiley.com/college/Seider)


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 www.wiley.com/college/Seider)


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 Make-or-Buy Decisions 570


19.4 Microeconomics of Product Development 572


19.5 Company and Societal Factors Affecting Product Development 573


19.6 Summary 574


References 575


Exercises 575


Chapter 20 Plantwide Controllability Assessment 576


20.0 Objectives 576


20.1 Introduction 576


20.2 Control System Configuration 579


20.3 Qualitative Plantwide Control System Synthesis 584


20.4 Summary 590


References 590


Exercises 591


20S Supplement to Chapter 20 (Online www.wiley.com/college/Seider)


20S.0 Objectives


20S.1 Generation of Linear Models in Standard Forms


20S.2 Quantitative Measures for Controllability and Resiliency


20S.3 Towards Automated Flowsheet C&R Diagnosis


20S.4 Control Loop Definition and Tuning


20S.5 Case Studies


Case Study 20S.1 Exothermic Reactor Design for the Production of Propylene Glycol


Case Study 20S.2 Two Alternative Heat Exchanger Networks


Case Study 20S.3 Interaction of design and Control in the MCB Separation Process


20S.6 MATLAB for C&R Analysis


20S.7 Summary


References


Exercises


Chapter 21 Design Optimization 597


21.0 Objectives 597


21.1 Introduction 597


21.2 General Formulation of the Optimization Problem 598


21.3 Classification of Optimization Problems 599


21.4 Linear Programming (LP) 601


21.5 Nonlinear Programming (NLP) with a Single Variable 603


21.6 Conditions for Nonlinear Programming (NLP) by Gradient Methods with Two or More Decision Variables 605


21.7 Optimization Algorithm 607


21.8 Flowsheet Optimizations—Case Studies 609


21.9 Summary 611


References 612


Exercises 612


Chapter 22 Optimal Design and Scheduling of Batch Processes 616


22.0 Objectives 616


22.1 Introduction 616


22.2 Design of Batch Process Units 617


22.3 Design of Reactor–Separator Processes 620


22.4 Design of Single-product Processing Sequences 622


22.5 Design on Multiproduct Processing Sequences 625


22.6 Summary 626


References 626


Exercises 627


PART FOUR DESIGN REPORTS—PRODUCT AND PROCESS 629


Chapter 23 Written Reports and Oral Presentations 631


23.0 Objectives 631


23.1 Contents of the Written Report 632


23.2 Preparation of the Written Report 636


23.3 Oral Design Presentations 638


23.4 Award Competition 641


23.5 Summary 641


References 641


PART FIVE CASE STUDIES—PRODUCT AND PROCESS DESIGNS 643


Chapter 24 Case Study 1—Home Hemodialysis Devices 645


24.0 Objectives 645


24.1 Hemodialysis Technology 645


24.2 Design Specifications of Home Hemodialysis Device 652


24.3 Summary 655


References 655


Bibliography Patents—Hemodialysis Devices—General 655


Patents—Hemodialysis Devices—Hollow-Fiber Membranes 656


Patents—Hemodialysis Devices—Dialysate Regeneration 656


Patents—Hemodialysis Devices—Alarms/User Interface 656


Exercises 656


Chapter 25 Case Study 2—High Throughput Screening Devices for Kinase Inhibitors 657


25.0 Objectives 657


25.1 Background Technology For High Throughput Screening of Kinase Inhibitors 657


25.2 Product Concept 665


25.3 Prototyping 669


25.4 Product Development 672


25.5 Summary 672


References 672


Patents 673


Exercises 673


Chapter 26 Case Study 3—Die Attach Adhesive: A Case Study of Product Development 674


26.0 Objectives 674


26.1 Background of Technology 674


26.2 Market Study 674


26.3 Product Design 677


26.4 Process Design 678


26.5 Prototyping 678


26.6 Estimation of Product Cost 679


26.7 Summary 680


References 680


Exercises 681


Chapter 27 Case Study 4—Ammonia Process 683


27.0 Objectives 683


27.1 Introduction 683


27.2 Initial Base Case Design 686


27.3 Design Refinement 692


Postscript 699


References 703


Exercises 703


APPENDICES


I. Residue Curves for Heterogeneous Systems 704


II. Design Problem Statements by Area 705


III. Materials of Construction 709


INDICES


Table of Acronyms 711


Author Index 719


Subject Index 725


NEW TO THIS EDITION

Approximately 100 video clips created by the authors within the enhanced eBook, each accompanied by quiz questions with answer-specific feedback

Expanded and new coverage of chemical product design, design optimization, engineering ethics, molecular and mixture design, mass integration, Six-Sigma design strategies, and more

Original and updated real-world case studies and supplemental resource material

Modern computer-based methods for process synthesis

Extensions and case studies that enhance the coverage of product design, especially of mixture blends, formulated products, and product devices

Updated and expanded resources available on the book companion site: program and simulation files that solve 60 example problems; a solution manual for homework exercises; 93 design problem statements, and multimedia courseware that uses voice, video, and animation to introduce new users of the steady-state simulators to the specifics of two of the most widely used process simulation programs, ASPEN PLUS and HYSYS (UniSim Design)


https://www.wiley.com/en-us/Product+and+Process+Design+Principles%3A+Synthesis%2C+Analysis+and+Evaluation%2C+4th+Edition-p-9781119282631#content-section

No comments:

Post a Comment