J.D.Seader is Professor 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.From 1952 to 1959，Seader designed processes for Chevron Research，and from 1959 to 1965，he conducted rocket engine reseach for Rocketdyne. Before joining the faculty at the University of Utah，he was a professor at the University of Idaho.Combined，he has authored or coauthored 102 technical articles，six books，and four patents，and also coauthored the section oh distillation in the 6th and 7th editions of Perrv’s Chemical Engineers’Handbook.Seader has been a trustee of CACHE for 26 years.serving as an executive Omcer from 1980 to 1984.For 20 years.he directed the use and distribution of Monsanto’S FLOⅥrTRAN process simulation computer program for various universities.Seader also served as a director 0f AlChE from 1983 to 1985.In 1983.he presented the 35th Annual Institute Lecture of AIChE，and in 1988，received the Computing in Chemical Engineering Award of the CAST Division of AIChE.
圖書目錄
Chapter 1 Separation Processes 1.1 Industrial Chemical Processes 1.2 Mechanism of Separation 1.3 Separation by Phase Addition or Creation 1.4 Separation by Barrier 1.5 Separation by Solid Agent 1.6 Separation by External Field of Gradient 1.7 Component Recoveries and PRODUCT purities 1.8 Separation Power 1.9 Selection of Feasible Separation Processes Chapter 2 Thermodynamics of Separation Operations 2.1 Energy，Entropy，and Availability Balances 2.2 Phase Equilibria 2.3 Ideal Gas，Ideal Liquid Solution Model 2.4 Graphical Correlations of Thermodynamic Properties 2.5 Nonideal Thermodynamic Property Models 2.6 Activity Coefficient Models for the Liquid Phase Chapter 3 Mass Transfer and Diffusion 3.1 Steady-State Ordinary Molecular Diffusion 3.2 Diffusion Coefficients 3.3 One-Dimensional Steady-State and Unsteady-State Molecular Diffusion 3.4 Molecular Diffusion in Laminar Flow 3.5 Mass Transfer in Turbulent Flow 3.6 Models for Mass Transfer at a Fluid-Fluid Interface 3.7 Two-Film Theory and Overall Mass Transfer Coefficients Chapter 4 Single Equilibrium Stages and Flash Calculations 4.1 The Gibbs Phase Rule and Degrees of Freedom 4.2 Binary Vapor-Liquid Systems 4.3 Azeotropic Systems 4.4 Multicomponent Flash，Bubble-Point，and Dew-Point Calculations 4.5 Ternary Liquid-Liquid Systems 4.6 Multicomponent Liquid-Liquid Systems 4.7 Solid-Liquid Systems 4.8 Gas-Liquid Systems 4.9 Gas-Solid Systems 4.10 Multiphase Systems Chapter 5 Cascades 5.1 Cascade Configurations 5.2 Solid-Liquid Cascades 5.3 Single-Section Liquid-Liquid Extraction Cascades 5.4 Multicomponent Vapor-Liquid Group Methods 5.5 Degrees of Freedom and Specifications for Countercurrent Cascades Chapter 6 Absorption and Stripping of Dilute Mixtures 6.1 Equipment 6.2 General Design Considerations 6.3 Graphical Equilibrium-Stage Method for Trayed Towers 6.4 Algebraic Method for Determining the Number of Equilibrium Stages 6.5 Stage Efficiency 6.6 Tray Capacity，Pressure Drop，and Mass Transfer 6.7 Rate-Based Method for Packed Columns 6.8 Packed Column Efficiency，Capacity， and Pressure Drop 6.9 Concentrated Solutions in Packed Columns Chapter 7 Distillation of Binary Mixtures 7.1 Equipment and Design Considerations 7.2 McCabe-Thiele Graphical Equilibrium-Stage Method for Trayed Towers 7.3 Estimation of Stage Efficiency 7.4 Capacity of Trayed Towers and Reflux Drums 7.5 Rate-Based Method for Packed Columns 7.6 Ponchon-Savarit Graphical Equilibrium-Stage Method for Trayed Towers Chapter 8 Liquid-Liquid Extraction with Ternary Systems Chapter 9 Approximate Methods for Multicomponent，Multistage Separtions Chapter 10 Equilibrium-Based Methods for Multicomponent Absorption，Stripping，Distillation，and Extraction Chapter 11 Enhanced Distillation and Supercritical Extraction Chapter 12 Rate-Based Models for Distillation Chapter 13 Batch Distillation Chapter 14 Membrane Separations Chapter 15 Adsorption，Ion Exchange，and Chromatography Index
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