Page 9 - Separation process engineering
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Example 10-1. Overall efficiency estimation
10.3. Column Diameter Calculations
Example 10-2. Diameter calculation for tray column
10.4. Balancing Calculated Diameters
10.5. Sieve Tray Layout and Tray Hydraulics
Example 10-3. Tray layout and hydraulics
10.6. Valve Tray Design
10.7. Introduction to Packed Column Design
10.8. Packed Column Internals
10.9. Height of Packing: HETP Method
10.10. Packed Column Flooding and Diameter Calculation
Example 10-4. Packed column diameter calculation
10.11. Economic Trade-Offs for Packed Columns
10.12. Choice of Column Type
10.13. Summary—Objectives
References
Homework
Appendix. Tray And Downcomer Design with Computer Simulator
Chapter 11 Economics and Energy Conservation in Distillation
11.1. Distillation Costs
11.2. Operating Effects on Costs
Example 11-1. Cost estimate for distillation
11.3. Changes in Plant Operating Rates
11.4. Energy Conservation in Distillation
11.5. Synthesis of Column Sequences for Almost Ideal Multicomponent Distillation
Example 11-2. Sequencing columns with heuristics
11.6. Synthesis of Distillation Systems for Nonideal Ternary Systems
Example 11-3. Process development for separation of complex ternary mixture
11.7. Summary—Objectives
References
Homework
Chapter 12 Absorption and Stripping
12.1. Absorption and Stripping Equilibria
12.2. McCabe-Thiele Solution for Dilute Absorption
Example 12-1. McCabe-Thiele analysis for dilute absorber
12.3. Stripping Analysis for Dilute Systems
12.4. Analytical Solution for Dilute Systems: Kremser Equation
Example 12-2. Stripping analysis with Kremser equation
12.5. Efficiencies