FREE SHIPPING BOTH WAYS
ON EVERY ORDER!
LIST PRICE:
$127.00

Sorry, this item is currently unavailable.

Equilibrium-Staged Separations : Separations in Chemical Engineering

ISBN: 9780135009680 | 0135009685
Format: Hardcover
Publisher: Prentice Hall PTR
Pub. Date: 1/1/1989

Why Rent from Knetbooks?

Because Knetbooks knows college students. Our rental program is designed to save you time and money. Whether you need a textbook for a semester, quarter or even a summer session, we have an option for you. Simply select a rental period, enter your information and your book will be on its way!

Top 5 reasons to order all your textbooks from Knetbooks:

  • We have the lowest prices on thousands of popular textbooks
  • Free shipping both ways on ALL orders
  • Most orders ship within 48 hours
  • Need your book longer than expected? Extending your rental is simple
  • Our customer support team is always here to help
SummaryTable of Contents
This volume provides concise, complete, single-volume coverage of the full spectrum of techniques for chemical separations, and focuses on a modern approach that integrates classical solutions with computer methods. Provides complete coverage of distillation, absorption, and extraction methods; and explains stage-by-stage techniques, matrix methods, and short-cut methods.MARKETS: For undergraduate Chemical Engineering students.
This book tries to satisfy the need of readers to learn about the standard separation me... MORE
Prefacexv(4)
Nomenclaturexix
Chapter 1. Introduction to Equilibrium-Staged Separations
1(8)
... MORE
1.1. Importance of Separations
1(1)
1.2. Problem-Solving Methods
2(2)
1.3. Prerequisite Material
4(1)
1.4. Summary -- Objectives
5(1)
References
6(1)
Homework
7(2)
Chapter 2. Vapor-Liquid Phase Equilibrium
9(32)
2.1. Concept of Equilibrium
9(1)
2.2. Form and Sources of Equilibrium Data
10(5)
2.3. Graphical Representation of Binary Equilibrium Data
15(6)
2.4. Graphical Mass Balances for Equilibrium Systems
21(2)
2.5. Other Representations of Equilibrium Data
23(6)
2.6. Calculation of Bubble-Point and Dew-Point Temperatures
29(4)
2.7. Summary -- Objectives
33(1)
References
34(2)
Homework
36(5)
Chapter 3. Flash Distillation
41(46)
3.1. Basic Method
41(1)
3.2. Binary Flash Distillation
42(9)
3.2.1. Sequential Solution Procedure
44(6)
3.2.2. Simultaneous Solution Procedure
50(1)
3.3. Multicomponent Flash Distillation
51(9)
3.4. Simultaneous Multicomponent Convergence
60(8)
3.4.1. Wide-Boiling Feeds
61(2)
3.4.2. Narrow-Boiling Feeds
63(5)
3.5. Size Calculation
68(5)
3.6. Utilizing Existing Flash Drums
73(1)
3.7. Summary -- Objectives
74(1)
References
75(1)
Homework
76(11)
Chapter 4. Introduction to Column Distillation
87(24)
4.1. Developing a Distillation Cascade
87(7)
4.2. Distillation Equipment
94(3)
4.3. Specifications
97(2)
4.4. External Column Balances
99(6)
4.5. Summary-Objectives
105(1)
Homework
105(6)
Chapter 5. Column Distillation: Internal Stage-by-stage Balances
111(46)
5.1. Internal Balances
111(6)
5.2. Binary Stage-by-stage Solution Methods
117(8)
5.3. Introduction to the McCabe-Thiele Method
125(5)
5.4. Feed Line
130(9)
5.5. Complete McCabe-Thiele Method
139(3)
5.6. Profiles
142(3)
5.7. Comparisons Between Analytical Lewis Method and Graphical McCabe-Thiele Diagram
145(2)
5.8. Summary -- Objectives
147(1)
References
148(1)
Homework
148(9)
Chapter 6. Advanced Binary Distillation: McCabe-Thiele and Lewis Analyses
157(58)
6.1. Example: Open Steam Distillation
157(5)
6.2. General Analysis Procedure
162(9)
6.3. Other Column Situations
171(6)
6.3.1. Partial Condensers
171(1)
6.3.2. Total Reboilers
172(1)
6.3.3. Side Streams
173(2)
6.3.4. Intermediate Reboilers and Intermediate Condensers
175(1)
6.3.5. Stripping and Enriching Columns
176(1)
6.4. Limiting Operating Conditions
177(3)
6.5. Efficiencies
180(2)
6.6. Simulation Problems
182(3)
6.7. New Uses for Old Columns
185(2)
6.8. Subcooled Reflux and Superheated Boilup
187(2)
6.9. Nonconstant Molal Overflow: Latent Heat Units
189(8)
6.10. Analytical and Computer Calculations
197(1)
6.11. Summary -- Objectives
198(1)
References
199(1)
Homework
199(16)
Chapter 7. Introduction to Multicomponent Distillation
215(18)
7.1. Calculational Difficulties
215(7)
7.2. Profiles
222(6)
7.3. Summary-Objectives
228(1)
Homework
228(5)
Chapter 8. Exact Calculation Procedures for Multicomponent Distillation
233(40)
8.1. Stage-By-Stage Calculations for Constant Molal Overflow
233(2)
8.2. Constant Relative Volatility Systems
235(5)
8.3. Bubble-Point or Dew-Point Calculations on Each Stage
240(10)
8.4. Nonconstant Molal Overflow
250(1)
8.5. Matrix Solution of Multicomponent Distillation
251(11)
8.5.1. Component Mass Balances
252(5)
8.5.2. Theta Method
257(2)
8.5.3. Energy Balances
259(3)
8.6. Summary -- Objectives
262(1)
References
263(1)
Homework
264(9)
Chapter 9. Approximate Shortcut Methods for Multicomponent Distillation
273(28)
9.1. Total Reflux: Fenske Equation
273(7)
9.2. Minimum Reflux: Underwood Equations
280(7)
9.3. Correlation for Number of Stages at Finite Reflux Ratio: Gilliland Correlation
287(4)
9.4. Summary -- Objectives
291(1)
References
291(1)
Homework
292(9)
Chapter 10. Introduction to Complex Distillation Methods
301(42)
10.1. Breaking Azeotropes with Other Separators
301(2)
10.2. Extractive Distillation
303(6)
10.3. Azeotropic Distillation Processes
309(18)
10.3.1. Binary Heterogeneous Azeotropes
309(3)
10.3.2. Drying Organic Compounds That Are Partially Miscible with Water
312(5)
10.3.3. Azeotropic Distillation with Added Solvent
317(5)
10.3.4. Steam Distillation
322(5)
10.4. Processes Using Changes in Pressure
327(2)
10.5. Distillation with Chemical Reaction
329(4)
10.6. Summary -- Objectives
333(1)
References
334(1)
Homework
335(8)
Chapter 11. Batch Distillation
343(26)
11.1. Mass Balances and Rayleigh Equation
345(1)
11.2. Simple Batch Distillation
346(5)
11.3. Batch Steam Distillation
351(2)
11.4. MultiStage Batch Distillation
353(6)
11.5. Operating Time
359(2)
11.6. Summary -- Objectives
361(1)
References
361(1)
Homework
362(7)
Chapter 12. Staged Column Design
369(44)
12.1. Staged Column Equipment Description
369(10)
12.1.1. Trays, Downcomers and Weirs
372(4)
12.1.2. Inlets and Outlets
376(3)
12.2. Tray Efficiencies
379(7)
12.3. Calculating the Column Diameter
386(6)
12.4. Sieve Tray Layout and Tray Hydraulics
392(10)
12.5. Valve Tray Design
402(2)
12.6. Summary -- Objectives
404(1)
References
405(2)
Homework
407(6)
Chapter 13. Packed Column Design
413(24)
13.1. Column Internals
413(5)
13.2. Height of Packing: HETP Approach
418(2)
13.3. Column Diameter
420(8)
13.4. Economic Trade-offs
428(1)
13.5. Summary -- Objectives
429(1)
References
430(1)
Homework
431(6)
Chapter 14. The Economics of Distillation and Energy Conservation in Distillation
437(34)
14.1. Capital and Operating Costs
437(5)
14.2. Calculation of Sizes and Costs
442(10)
14.3. Changes in Plant Operating Rates
452(1)
14.4. Energy Conservation in Distillation Columns
453(5)
14.5. Coupling of Columns for Multicomponent Purifications
458(5)
14.6. Summary -- Objectives
463(1)
References
464(3)
Homework
467(4)
Chapter 15. Absorption and Stripping
471(44)
15.1. Absorption and Stripping Equilibria
473(3)
15.2. Operating Lines for Absorption
476(6)
15.3. Stripping Analysis
482(2)
15.4. Column Diameter
484(1)
15.5. Analytical Solution: Kremser Equation
485(9)
15.6. Dilute Multisolute Absorbers and Strippers
494(3)
15.7. Matrix Solution
497(5)
15.8. Irreversible Absorption
502(2)
15.9. Summary -- Objectives
504(1)
References
504(2)
Homework
506(9)
Chapter 16. Immiscible Extraction
515(34)
16.1. Extraction Processes and Equipment
515(1)
16.2. Countercurrent Extraction
516(14)
16.2.1. McCabe-Thiele Method
520(9)
16.2.2. Kremser Method
529(1)
16.3. Fractional Extraction
530(5)
16.4. Cross Flow and Two-Dimensional Systems
535(5)
16.5. Summary -- Objectives
540(1)
References
540(2)
Homework
542(7)
Chapter 17. Extending McCabe-Thiele Analysis and the Kremser Equation to Other Separations
549(26)
17.1. Generalized McCabe-Thiele Procedure
549(2)
17.2. Washing
551(7)
17.3. Leaching
558(3)
17.4. Supercritical Fluid Extraction
561(3)
17.5. Three-Phase Systems
564(3)
17.6. Application to Other Separations
567(1)
17.7. Summary -- Objectives
567(1)
References
568(1)
Homework
569(6)
Chapter 18. Extraction of Partially Miscible Systems
575(60)
18.1. Extraction Equilibria
575(4)
18.2. Mixing Calculations and the Lever-Arm Rule
579(3)
18.3. Single-Stage and Cross-Flow Systems
582(4)
18.4. Countercurrent Extraction Cascades
586(11)
18.4.1. External Mass Balances
586(3)
18.4.2. Difference Points and Stage-by-Stage Calculations
589(6)
18.4.3. Complete Extraction Problem
595(2)
18.5. Relationship Between McCabe-Thiele and Triangular Diagrams
597(2)
18.6. Computer Calculations
599(2)
18.7. Effect of Solvent Rate
601(2)
18.8. Simulation Problems
603(1)
18.9. Two-Feed Extraction Column
604(7)
18.10. Extract Reflux
611(8)
18.10.1. Extract Reflux Ratio
615(4)
18.11. Leaching
619(4)
18.12. Summary -- Objectives
623(1)
References
623(1)
Homework
624(11)
Chapter 19. Mass Transfer Analysis
635(60)
19.1. Basics of Mass Transfer
635(4)
19.2. Distillation
639(9)
19.3. Relationship Between HETP and HTU
648(3)
19.4. Mass Transfer Correlations for Packed Towers
651(10)
19.4.1. Detailed Correlations
651(9)
19.4.2. Simple Correlations
660(1)
19.5. Absorbers and Strippers
661(7)
19.6. Cocurrent Absorbers
668(2)
19.7. Mass Transfer on a Stage
670(4)
19.8. Cooling Towers, Humidification, and Dehumidification
674(14)
19.9. Summary -- Objectives
688(1)
References
688(2)
Homework
690(5)
Index695

Related Products


  • Separation Process Engineering
    Separation Process Engineering
  • Separation Process Engineering : Includes Mass Transfer Analysis
    Separation Process Engineering...


Please wait while this item is added to your cart...