Book description
The Definitive, Up-to-Date, Student-Friendly Guide to Separation Process Engineering—With More Mass Transfer Coverage and a New Chapter on Crystallization
Separation Process Engineering, Fourth Edition, is the most comprehensive, accessible guide available on modern separation processes and the fundamentals of mass transfer. In this completely updated edition, Phillip C. Wankat teaches each key concept through detailed, realistic examples using real data—including up-to-date simulation practice and spreadsheet-based exercises.
Wankat thoroughly covers each separation process, including flash, column, and batch distillation; exact calculations and shortcut methods for multicomponent distillation; staged and packed column design; absorption; stripping; and more. This edition provides expanded coverage of mass transfer and diffusion, so faculty can cover separations and mass transfer in one course.
Detailed discussions of liquid-liquid extraction, adsorption, chromatography, and ion exchange prepare students for advanced work. Wankat presents coverage of membrane separations, including gas permeation, reverse osmosis, ultrafiltration, pervaporation, and applications. An updated chapter on economics and energy conservation in distillation adds coverage of equipment costs.
This edition contains more than 300 new, up-to-date homework problems, extensively tested in undergraduate courses at Purdue University and the University of Canterbury (New Zealand).
Coverage includes
New chapter on crystallization from solution, including equilibrium, chemical purity, crystal size distribution, and pharmaceutical applications
Thirteen up-to-date Aspen Plus process simulation labs, adaptable to any simulator
Eight detailed Aspen Chromatography labs
Extensive new coverage of ternary stage-by-stage distillation calculations
Fraction collection and multicomponent calculations for simple batch distillation
New mass transfer analysis sections on numerical solution for variable diffusivity
Mass transfer to expanding or contracting objects, including ternary mass transfer
Expanded coverage of pervaporation
Updated Excel spreadsheets offering more practice with distillation, diffusion, mass transfer, and membrane separation problems
Table of contents
- Cover Page
- About This E-Book
- Title Page
- Copyright Page
- Dedication Page
- Contents
- Preface
- Acknowledgments
- About the Author
- Nomenclature
- Chapter 1. Introduction to Separation Process Engineering
-
Chapter 2. Flash Distillation
- 2.0 Summary—Objectives
- 2.1 Basic Method of Flash Distillation
- 2.2 Form and Sources of Equilibrium Data
- 2.3 Graphical Representation of Binary VLE
- 2.4 Binary Flash Distillation
- 2.5 Multicomponent VLE
- 2.6 Multicomponent Flash Distillation
- 2.7 Simultaneous Multicomponent Convergence
- 2.8 Three-Phase Flash Calculations
- 2.9 Size Calculation
- 2.10 Using Existing Flash Drums
- References
- Homework
- Chapter 2. Appendix A. Computer Simulation of Flash Distillation
- Chapter 2 Appendix B. Spreadsheets for Flash Distillation
- Chapter 3. Introduction to Column Distillation
-
Chapter 4. Binary Column Distillation: Internal Stage-by-Stage Balances
- 4.0 Summary—Objectives
- 4.1 Internal Balances
- 4.2 Binary Stage-by-Stage Solution Methods
- 4.3 Introduction to the McCabe-Thiele Method
- 4.4 Feed Line
- 4.5 Complete McCabe-Thiele Method
- 4.6 Profiles for Binary Distillation
- 4.7 Open Steam Heating
- 4.8 General McCabe-Thiele Analysis Procedure
- 4.9 Other Distillation Column Situations
- 4.10 Limiting Operating Conditions
- 4.11 Efficiencies
- 4.12 Simulation Problems
- 4.13 New Uses for Old Columns
- 4.14 Subcooled Reflux and Superheated Boilup
- 4.15 Comparisons Between Analytical and Graphical Methods
- References
- Homework
- Chapter 4 Appendix A. Computer Simulation of Binary Distillation
- Chapter 4 Appendix B. Spreadsheets for Binary Distillation
-
Chapter 5. Introduction to Multicomponent Distillation
- 5.0 Summary—Objectives
- 5.1 Calculational Difficulties
- 5.2 Profiles for Multicomponent Distillation
- 5.3 Stage-by-Stage Calculations for CMO
- References
- Homework
- Chapter 5 Appendix A. Simplified Spreadsheet for Stage-by-Stage Calculations for Ternary Distillation
- Chapter 5 Appendix B. Automated Spreadsheet with VBA for Stage-by-Stage Calculations for Ternary Distillation
-
Chapter 6. Exact Calculation Procedures for Multicomponent Distillation
- 6.0 Summary—Objectives
- 6.1 Introduction to Matrix Solution for Multicomponent Distillation
- 6.2 Component Mass Balances in Matrix Form
- 6.3 Initial Guesses for Flow Rates and Temperatures
- 6.4 Temperature Convergence
- 6.5 Energy Balances in Matrix Form
- 6.6 Introduction to Naphtali-Sandholm Simultaneous Convergence Method
- 6.7 Discussion
- References
- Homework
- Chapter 6 Appendix. Computer Simulations for Multicomponent Column Distillation
- Chapter 7. Approximate Shortcut Methods for Multicomponent Distillation
-
Chapter 8. Introduction to Complex Distillation Methods
- 8.0 Summary—Objectives
- 8.1 Breaking Azeotropes with Other Separators
- 8.2 Binary Heterogeneous Azeotropic Distillation Processes
- 8.3 Steam Distillation
- 8.4 Pressure-Swing Distillation Processes
- 8.5 Complex Ternary Distillation Systems
- 8.6 Extractive Distillation
- 8.7 Azeotropic Distillation with Added Solvent
- 8.8 Distillation with Chemical Reaction
- References
- Homework
- Chapter 8 Appendix A. Simulation of Complex Distillation Systems
- Chapter 8 Appendix B. Spreadsheet for Residue Curve Generation
-
Chapter 9. Batch Distillation
- 9.0 Summary—Objectives
- 9.1 Introduction to Batch Distillation
- 9.2 Batch Distillation: Rayleigh Equation
- 9.3 Simple Binary Batch Distillation
- 9.4 Constant-Mole Batch Distillation
- 9.5 Batch Steam Distillation
- 9.6 Multistage Binary Batch Distillation
- 9.7 Multicomponent Simple Batch Distillation
- 9.8 Operating Time
- References
- Homework
- Chapter 9 Appendix A. Spreadsheet for Simple Multicomponent Batch Distillation, Constant Relative Volatility
-
Chapter 10. Staged and Packed Column Design
- 10.0 Summary—Objectives
- 10.1 Staged Column Equipment Description
- 10.2 Tray Efficiencies
- 10.3 Column Diameter Calculations
- 10.4 Balancing Calculated Diameters
- 10.5 Sieve Tray Layout and Tray Hydraulics
- 10.6 Valve Tray Design
- 10.7 Introduction to Packed Column Design
- 10.8 Packings and Packed Column Internals
- 10.9 Height of Packing: HETP Method
- 10.10 Packed Column Flooding and Diameter Calculation
- 10.11 Economic Trade-Offs for Packed Columns
- 10.12 Choice of Column Type
- References
- Homework
- Chapter 10 Appendix. Tray and Downcomer Design with Computer Simulator
-
Chapter 11. Economics and Energy Conservation in Distillation
- 11.0 Summary—Objectives
- 11.1 Equipment Costs
- 11.2 Basic Heat Exchanger Design
- 11.3 Design and Operating Effects on Costs
- 11.4 Changes in Plant Operating Rates
- 11.5 Energy Conservation in Distillation
- 11.6 Synthesis of Column Sequences for Almost Ideal Multicomponent Distillation
- 11.7 Synthesis of Distillation Systems for Nonideal Ternary Systems
- References
- Homework
-
Chapter 12. Absorption and Stripping
- 12.0 Summary—Objectives
- 12.1 Absorption and Stripping Equilibria
- 12.2 McCabe-Thiele Solution for Dilute Absorption
- 12.3 Stripping Analysis for Dilute Systems
- 12.4 Analytical Solution for Dilute Systems: Kremser Equation
- 12.5 Efficiencies
- 12.6 McCabe-Thiele Analysis for More Concentrated Systems
- 12.7 Column Diameter
- 12.8 Dilute Multisolute Absorbers and Strippers
- 12.9 Matrix Solution for Concentrated Absorbers and Strippers
- 12.10 Irreversible Absorption and Cocurrent Cascades
- References
- Homework
- Chapter 12 Appendix. Computer Simulations of Absorption and Stripping
-
Chapter 13. Liquid-Liquid Extraction
- 13.0 Summary—Objectives
- 13.1 Extraction Processes and Equipment
- 13.2 Dilute, Immiscible, Countercurrent Extraction
- 13.3 Dilute Fractional Extraction
- 13.4 Immiscible Single-Stage and Cross-Flow Extraction
- 13.5 Concentrated Immiscible Extraction
- 13.6 Immiscible Batch Extraction
- 13.7 Extraction Equilibrium for Partially Miscible Ternary Systems
- 13.8 Mixing Calculations and the Lever-Arm Rule
- 13.9 Partially Miscible Single-Stage and Cross-Flow Systems
- 13.10 Countercurrent Extraction Cascades for Partially Miscible Systems
- 13.11 Relationship Between McCabe-Thiele and Triangular Diagrams for Partially Miscible Systems
- 13.12 Minimum Solvent Rate for Partially Miscible Systems
- 13.13 Extraction Computer Simulations
- 13.14 Design of Mixer-Settlers
- References
- Homework
- Chapter 13 Appendix. Computer Simulation of Extraction
-
Chapter 14. Washing, Leaching, and Supercritical Extraction
- 14.0 Summary—Objectives
- 14.1 Generalized McCabe-Thiele and Kremser Procedures
- 14.2 Washing
- 14.3 Leaching with Constant Flow Rates
- 14.4 Leaching with Variable Flow Rates
- 14.5 Introduction to Supercritical Fluid Extraction
- 14.6 Application of McCabe-Thiele and Kremser Methods to Other Separations
- References
- Homework
-
Chapter 15. Introduction to Diffusion and Mass Transfer
- 15.0 Summary–Objectives
- 15.1 Molecular Movement Leads to Mass Transfer
- 15.2 Fickian Model of Diffusivity
- 15.3 Values and Correlations for Fickian Binary Diffusivities
- 15.4 Linear Driving-Force Model of Mass Transfer for Binary Systems
- 15.5 Correlations for Mass Transfer Coefficients
- 15.6 Difficulties with Fickian Diffusion Model
-
15.7 Maxwell-Stefan Model of Diffusion and Mass Transfer
- 15.7.1 Introductory Development of the Maxwell-Stefan Theory of Diffusion
- 15.7.2 Maxwell-Stefan Equations for Binary Nonideal Systems
- 15.7.3 Determining Independent Fluxes Nj,z
- 15.7.4 Maxwell-Stefan Difference Equation Formulations
- 15.7.5 Relationship between Maxwell-Stefan and Fickian Diffusivities
- 15.7.6 Ideal Ternary Systems
- 15.7.7 Ternary Mass Transfer to Expanding or Contracting Objects
- 15.7.8 Nonideal Ternary Systems
- 15.8 Advantages and Disadvantages of Different Diffusion and Mass Transfer Models
- References
- Homework
- Chapter 15 Appendix. Spreadsheets Examples 15-10 and 15-11
-
Chapter 16. Mass Transfer Analysis for Distillation, Absorption, Stripping, and Extraction
- 16.0 Summary—Objectives
- 16.1 HTU-NTU Analysis of Packed Distillation Columns
- 16.2 Relationship of HETP and HTU
- 16.3 Mass Transfer Correlations for Packed Towers
- 16.4 HTU-NTU Analysis of Concentrated Absorbers and Strippers
- 16.5 HTU-NTU Analysis of CoCurrent Absorbers
- 16.6 Prediction of Distillation Tray Efficiency
- 16.7 Mass Transfer Analysis of Extraction
- 16.8 Rate-Based Analysis of Distillation
- References
- Homework
- Chapter 16 Appendix. Computer Rate-Based Simulation of Distillation
-
Chapter 17. Crystallization from Solution
- 17.0 Summary–Objectives
- 17.1 Basic Principles of Crystallization from Solution
- 17.2 Continuous Cooling Crystallizers
- 17.3 Evaporative and Vacuum Crystallizers
- 17.4 Sieve Analysis
- 17.5 Introduction to Population Balances
- 17.6 Crystal Size Distributions for MSMPR Crystallizers
- 17.7 Seeding
- 17.8 Batch and Semibatch Crystallization
- 17.9 Precipitation
- References
- Homework
- Chapter 17 Appendix. Spreadsheets
- Chapter 18. Introduction to Membrane Separation Processes
-
Chapter 19. Introduction to Adsorption, Chromatography, and Ion Exchange
- 19.0 Summary—Objectives
- 19.1 Sorbents and Sorption Equilibrium
- 19.2 Solute Movement Analysis for Linear Systems: Basics and Applications to Chromatography
- 19.3 Solute Movement Analysis for Linear Systems: Temperature and Pressure Swing Adsorption and Simulated Moving Beds
- 19.4 Nonlinear Solute Movement Analysis
- 19.5 Ion Exchange
- 19.6 Mass and Energy Transfer in Packed Beds
- 19.7 Mass Transfer Solutions for Linear Systems
- 19.8 LUB Approach for Nonlinear Sorption Systems
- 19.9 Checklist for Practical Design and Operation
- References
- Homework
- Chapter 19 Appendix. Aspen Chromatography Simulator
- Appendix A. Aspen Plus Troubleshooting Guide for Separations
- Appendix B. Instructions for Fitting VLE and LLE Data with Aspen Plus
- Appendix C. Unit Conversions and Physical Constants
- Appendix D. Data Locations
- Answers to Selected Problems
- Index
- Code Snippets
Product information
- Title: Separation Process Engineering: Includes Mass Transfer Analysis, 4th Edition
- Author(s):
- Release date: August 2016
- Publisher(s): Pearson
- ISBN: 9780133443714
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