Page 12 - Separation process engineering
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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 the Independent Fluxes N i,z
15.7.4. Difference Equation Formulations
15.7.5. Relationship between Maxwell-Stefan and Fickian Diffusivities
Example 15-5. Maxwell-Stefan nonideal binary diffusion
15.7.6. Ideal Ternary Systems
Example 15-6. Maxwell-Stefan ideal ternary system
15.7.7. Nonideal Ternary Systems
15.8. Advantages and Disadvantages of Different Diffusion and Mass-Transfer Models
15.9. Summary—Objectives
References
Homework
Appendix. Spreadsheet for Example 15-6
Chapter 16 Mass Transfer Analysis for Distillation, Absorption, Stripping, and Extraction
16.1. HTU-NTU Analysis of Packed Distillation Columns
Example 16-1. Distillation in a packed column
16.2. Relationship of HETP and HTU
16.3. Mass Transfer Correlations for Packed Towers
16.3.1. Detailed Correlations for Random Packings
Example 16-2. Estimation of HG and HL
16.3.2. Simple Correlations for the Random Packings
16.4. HTU-NTU Analysis of Absorbers and Strippers
Example 16-3. Absorption of SO2
16.5. HTU-NTU Analysis of Co-Current Absorbers
16.6. Prediction of Distillation Tray Efficiency
Example 16-4. Estimation of stage efficiency
16.7. Mass-Transfer Analysis of Extraction
16.7.1. Mass-Transfer Equations and HTU-NTU Analysis
16.7.2. Calculation of Stage Efficiency in Extraction Mixers
Example 16.5. Conversion of mass-transfer coefficients and estimation of stage efficiency in
mixer
16.7.3. Area per Volume a and Average Drop Diameter in Mixers
16.7.4. Mixer Mass-Transfer Coefficients
16.7.4.1. Mixer Mass-Transfer Coefficients for Individual Drops (Optional)
16.7.4.2. Mass-Transfer Coefficients for Drop Swarms in Mixers
16.7.4.3. Conservative Estimation of Mass-Transfer Coefficients for Extraction
Example 16-6. Conservative estimation of mixer mass-transfer coefficients
16.8. Rate-Based Analysis of Distillation
