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9780471586265

Separation Process Principles

by ;
  • ISBN13:

    9780471586265

  • ISBN10:

    0471586269

  • Edition: 1st
  • Format: Hardcover
  • Copyright: 1998-01-01
  • Publisher: Wiley

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Summary

This book examines rate-based and equilibrium-based approaches to separation operations. It describes the fundamentals of all separation operations of commercial interest, and includes theory and application examples in each chapter, as well as over 600 exercises.

Table of Contents

Chapter 1 Separation Processes
1(30)
1.1 Industrial Chemical Processes
1(4)
1.2 Mechanism of Separation
5(2)
1.3 Separation by Phase Addition or Creation
7(7)
1.4 Separation by Barrier
14(2)
1.5 Separation by Solid Agent
16(2)
1.6 Separation by External Field or Gradient
18(1)
1.7 Component Recoveries and Product Purities
19(3)
1.8 Separation Power
22(1)
1.9 Selection of Feasible Separation Processes
23(4)
Summary
27(1)
References
28(1)
Exercises
28(3)
Chapter 2 Thermodynamics of Separation Operations
31(59)
2.1 Energy, Entropy, and Availability Balances
31(59)
2.2 Phase Equilibria
36(6)
Fugacities and Activity Coefficients
37(1)
K-Values
38(4)
2.3 Ideal Gas, Ideal Liquid Solution Model
42(5)
2.4 Graphical Correlations of Thermodynamic Properties
47(4)
2.5 Nonideal Thermodynamic Property Models
51(12)
P-v-T Equation-of-State Models
54(4)
Derived Thermodynamic Properties from P-v-T Models
58(5)
2.6 Activity Coefficient Models for the Liquid Phase
63(20)
Activity Coefficients from Gibbs Free Energy
63(1)
Regular Solution Model
64(2)
Chao-Seader Correlation
66(2)
Nonideal Liquid Solutions
68(4)
Margules Equations
72(1)
van Laar Equation
72(2)
Local Composition Concept and Wilson Equation
74(4)
NRTL Equation
78(1)
UNIQUAC Equation
79(1)
UNIFAC Equation
80(2)
Liquid-Liquid Equilibria
82(1)
Summary
83(1)
References
83(1)
Exercises
84(6)
Chapter 3 Mass Transfer and Diffusion
90(73)
3.1 Steady-State Ordinary Molecular Diffusion
91(8)
Fick's Law of Diffusion
92(1)
Velocities in Mass Transfer
92(1)
Equimolar Counterdiffusion
93(2)
Unimolecular Diffusion
95(4)
3.2 Diffusion Coefficients
99(18)
Diffusivity in Gas Mixtures
99(2)
Diffusivity in Liquid Mixtures
101(8)
Diffusivity in Solids
109(8)
3.3 One-Dimensional Steady-State and Unsteady-State Molecular Diffusion
117(9)
Steady State
117(1)
Unsteady State
118(8)
3.4 Molecular Diffusion in Laminar Flow
126(14)
Falling Liquid Film
127(6)
Boundary-Layer Flow on a Flat Plate
133(3)
Fully Developed Flow in a Straight, Circular Tube
136(4)
3.5 Mass Transfer in Turbulent Flow
140(4)
Reynolds Analogy
141(1)
Chilton-Colburn Analogy
142(1)
Prandtl Analogy
143(1)
3.6 Models for Mass Transfer at a Fluid-Fluid Interface
144(6)
Film Theory
145(1)
Penetration Theory
146(1)
Surface Renewal Theory
147(2)
Film-Penetration Theory
149(1)
3.7 Two-Film Theory and Overall Mass Transfer Coefficients
150(7)
Gas-Liquid Case
150(3)
Liquid-Liquid Case
153(1)
Case of Large Driving Forces for Mass Transfer
154(3)
Summary
157(1)
References
158(1)
Exercises
159(4)
Chapter 4 Single Equilibrium Stages and Flash Calculations
163(69)
4.1 The Gibbs Phase Rule and Degrees of Freedom
163(3)
Degrees-of-Freedom Analysis
164(2)
4.2 Binary Vapor-Liquid Systems
166(7)
4.3 Azeotropic Systems
173(3)
4.4 Multicomponent Flash, Bubble-Point, and Dew-Point Calculations
176(10)
Isothermal Flash
178(3)
Bubble and Dew Points
181(3)
Adiabatic Flash
184(2)
4.5 Ternary Liquid-Liquid Systems
186(9)
4.6 Multicomponent Liquid-Liquid Systems
195(3)
4.7 Solid-Liquid Systems
198(9)
Leaching
198(3)
Crystallization
201(3)
Liquid Adsorption
204(3)
4.8 Gas-Liquid Systems
207(4)
4.9 Gas-Solid Systems
211(2)
Sublimation and Desublimation
211(1)
Gas Adsorption
212(1)
4.10 Multiphase Systems
213(7)
Approximate Method for a Vapor-Liquid-Solid System
214(1)
Approximate Method for a Vapor-Liquid-Liquid System
215(3)
Rigorous Method for a Vapor-Liquid-Liquid System
218(2)
Summary
220(1)
References
221(1)
Exercises
222(10)
Chapter 5 Cascades
232(38)
5.1 Cascade Configurations
232(2)
5.2 Solid-Liquid Cascades
234(3)
5.3 Single-Section Liquid-Liquid Extraction Cascades
237(4)
Cocurrent Cascade
238(1)
Crosscurrent Cascade
239(1)
Countercurrent Cascade
239(2)
5.4 Multicomponent Vapor-Liquid Cascades
241(12)
Single-Section Cascades by Group Methods
242(4)
Two-Section Cascades
246(7)
5.5 Degrees of Freedom and Specifications for Countercurrent Cascades
253(10)
Stream Variables
254(1)
Adiabatic or Nonadiabatic Equilibrium Stage
254(1)
Single-Section Countercurrent Cascade
255(2)
Two-Section Countercurrent Cascades
257(6)
Summary
263(1)
References
264(1)
Exercises
264(6)
Chapter 6 Absorption and Stripping of Dilute Mixtures
270(85)
6.1 Equipment
273(8)
6.2 General Design Considerations
281(1)
6.3 Graphical Equilibrium-Stage Method for Trayed Towers
282(7)
Minimum Absorbent Flow Rate
284(1)
Number of Equilibrium Stages
285(4)
6.4 Algebraic Method for Determining the Number of Equilibrium Stages
289(3)
6.5 Stage Efficiency
292(13)
Performance Data
293(1)
Empirical Correlations
294(5)
Semitheoretical Models
299(4)
Scale-up from Laboratory Data
303(2)
6.6 Tray Capacity, Pressure Drop, and Mass Transfer
305(12)
Tray Diameter
306(4)
Tray Vapor Pressure Drop
310(2)
Mass Transfer Coefficients and Transfer Units
312(3)
Weeping, Entrainment, and Downcomer Backup
315(2)
6.7 Rate-Based Method for Packed Columns
317(8)
6.8 Packed Column Efficiency, Capacity, and Pressure Drop
325(17)
Liquid Holdup
325(5)
Capacity and Pressure Drop
330(5)
Mass Transfer Efficiency
335(7)
6.9 Concentrated Solutions in Packed Column
342(4)
Summary
346(1)
References
347(1)
Exercises
348(7)
Chapter 7 Distillation of Binary Mixtures
355(64)
7.1 Equipment and Design Considerations
358(1)
7.2 McCabe-Thiele Graphical Equilibrium-Stage Method for Trayed Towers
359(32)
Rectifying Section
362(3)
Stripping Section
365(1)
Feed-Stage Considerations
366(3)
Determination of Number of Equilibrium Stages and Feed-Stage Location
369(1)
Limiting Conditions
369(5)
Column Operating Pressure and Condenser Type
374(2)
Subcooled Reflux
376(4)
Reboiler Type
380(1)
Condenser and Reboiler Duties
381(1)
Feed Preheat
382(1)
Optimal Reflux Ratio
382(2)
Large Number of Stages
384(2)
Use of Murphree Efficiency
386(1)
Multiple Feeds, Side Streams, and Open Steam
387(4)
7.3 Estimation of Stage Efficiency
391(6)
Performance Data
391(1)
Empirical Correlations
392(3)
Semitheoretical Models
395(1)
Scale-up from Laboratory Data
396(1)
7.4 Capacity of Trayed Towers and Reflux Drums
397(1)
Reflux Drums
397(1)
7.5 Rate-Based Method for Packed Columns
398(6)
HETP Method
399(1)
HTU Method
400(4)
7.6 Ponchon-Savarit Graphical Equilibrium-Stage Method for Trayed Towers
404(2)
Summary
406(1)
References
407(1)
Exercises
408(11)
Chapter 8 Liquid-Liquid Extraction with Ternary Systems
419(73)
8.1 Equipment
423(9)
Mixer-Settlers
424(2)
Spray Columns
426(1)
Packed Columns
426(1)
Plate Columns
426(1)
Columns with Mechanically Assisted Agitation
427(5)
8.2 General Design Considerations
432(6)
8.3 Hunter and Nash Graphical Equilibrium-Stage Method
438(21)
Number of Equilibrium Stages
440(4)
Minimum and Maximum Solvent-to-Feed Flow-Rate Ratios
444(4)
Use of Right-Triangle Diagrams
448(3)
Use of an Auxiliary Distribution Curve
451(2)
Extract and Raffinate Reflux
453(6)
8.4 Maloney and Schubert Graphical Equilibrium-Stage Method
459(6)
8.5 Theory and Scale-up of Extractor Performance
465(19)
Mixer-Settler Units
465(10)
Multicompartment Columns
475(5)
Axial Dispersion
480(4)
Summary
484(1)
References
485(1)
Exercises
486(6)
Chapter 9 Approximate Methods for Multicomponent, Multistage Separations
492(34)
9.1 Fenske-Underwood-Gilliland Method
492(22)
Selection of Two Key Components
493(2)
Column Operating Pressure
495(2)
Fenske Equation for Minimum Equilibrium Stages
497(3)
Distribution of Nonkey Components at Total Reflux
500(1)
Underwood Equations for Minimum Reflux
501(7)
Gilliland Correlation for Actual Reflux Ratio and Theoretical Stages
508(3)
Feed-Stage Location
511(1)
Distribution of Nonkey Components at Actual Reflux
512(2)
9.2 Kremser Group Method
514(7)
Strippers
514(4)
Liquid-Liquid Extraction
518(3)
Summary
521(1)
References
521(1)
Exercises
522(4)
Chapter 10 Equilibrium-Based Methods for Multicomponent Absorption, Stripping, Distillation, and Extraction
526(60)
10.1 Theoretical Model for an Equilibrium Stage
526(4)
10.2 General Strategy of Mathematical Solution
530(1)
10.3 Equation-Tearing Procedures
531(24)
Tridiagonal Matrix Algorithm
531(3)
Bubble-Point Method for Distillation
534(10)
Sum-Rates Method for Absorption and Stripping
544(7)
Isothermal Sum-Rates Method for Liquid-Liquid Extraction
551(4)
10.4 Simultaneous Correction Procedures
555(14)
10.5 Inside-Out Method
569(8)
MESH Equations
571(1)
Rigorous and Complex Thermodynamic Property Models
571(1)
Approximate Thermodynamic Property Models
572(1)
Inside-Out Algorithm
573(4)
Summary
577(1)
References
578(1)
Exercises
579(7)
Chapter 11 Enhanced Distillation and Supercritical Extraction
586(69)
11.1 Use of Triangular Graphs
587(17)
Residue-Curve Maps
591(8)
Distillation-Curve Maps
599(3)
Product-Composition Regions at Total Reflux
602(2)
11.2 Extractive Distillation
604(7)
11.3 Salt Distillation
611(1)
11.4 Pressure-Swing Distillation
612(4)
11.5 Homogeneous Azeotropic Distillation
616(5)
11.6 Heterogeneous Azeotropic Distillation
621(10)
Multiplicity
627(4)
11.7 Reactive Distillation
631(10)
11.8 Supercritical-Fluid Extraction
641(9)
Summary
650(1)
References
651(2)
Exercises
653(2)
Chapter 12 Rate-Based Models for Distillation
655(26)
12.1 Rate-Based Model
658(4)
12.2 Thermodynamic Properties and Transport-Rate Expressions
662(5)
12.3 Methods for Estimating Transport Coefficients and Interfacial Area
667(1)
12.4 Vapor and Liquid Flow Patterns
668(1)
12.5 Method of Calculation
668(9)
ChemSep Program
668(6)
RATEFRAC Program
674(3)
Summary
677(1)
References
677(1)
Exercises
677(4)
Chapter 13 Batch Distillation
681(32)
13.1 Differential Distillation
681(4)
13.2 Binary Batch Rectification with Constant Reflux and Variable Distillate Composition
685(3)
13.3 Binary Batch Rectification with Constant Distillate Composition and Variable Reflux
688(1)
13.4 Batch Stripping and Complex Batch Distillation
689(2)
13.5 Effect of Liquid Holdup
691(1)
13.6 Shortcut Method for Multicomponent Batch Rectification with Constant Reflux
691(4)
13.7 Stage-by-Stage Methods for Multicomponent Batch Rectification
695(13)
Rigorous Model
695(3)
Rigorous Integration Method
698(7)
Rapid Solution Method
705(3)
Summary
708(1)
References
708(1)
Exercises
709(4)
Chapter 14 Membrane Separations
713(65)
14.1 Membrane Materials
718(4)
14.2 Membrane Modules
722(3)
14.3 Transport in Membranes
725(22)
Porous Membranes
725(1)
Bulk Flow
726(2)
Liquid Diffusion
728(1)
Gas Diffusion
729(2)
Nonporous Membranes
731(1)
Solution-Diffusion for Liquid Mixtures
731(2)
Solution-Diffusion for Gas Mixtures
733(5)
Module Flow Patterns
738(3)
Cascades
741(4)
Concentration Polarization
745(2)
14.4 Dialysis and Electrodialysis
747(8)
Electrodialysis
750(5)
14.5 Reverse Osmosis
755(6)
14.6 Gas Permeation
761(4)
14.7 Pervaporation
765(6)
Summary
771(2)
References
773(1)
Exercises
773(5)
Chapter 15 Adsorption, Ion Exchange, and Chromatography
778(103)
15.1 Sorbents
781(13)
Adsorbents
782(7)
Ion Exchangers
789(3)
Sorbents for Chromatography
792(2)
15.2 Equilibrium Considerations
794(17)
Pure Gas Adsorption
794(8)
Liquid Adsorption
802(4)
Ion Exchange Equilibria
806(4)
Equilibria in Chromatography
810(1)
15.3 Kinetic and Transport Considerations
811(9)
External Transport
812(4)
Internal Transport
816(2)
Mass Transfer in Ion Exchange and Chromatography
818(2)
15.4 Sorption Systems
820(50)
Adsorption
820(4)
Ion Exchange
824(1)
Chromatography
825(2)
Slurry Adsorption (Contact Filtration)
827(4)
Fixed-Bed Adsorption (Percolation)
831(12)
Thermal-Swing Adsorption
843(5)
Pressure-Swing Adsorption
848(8)
Continuous Countercurrent Adsorption Systems
856(5)
Ion-Exchange Cycle
861(2)
Chromatographic Separations
863(7)
Summary
870(2)
References
872(1)
Exercises
873(8)
Index 881

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