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Distillation Engineering (Hardcover)
Loot Price: R3,545
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Distillation Engineering (Hardcover)
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Partial Table of Contents I. The Thermal Separation of Liquids II.
Thermodynamics of Mixtures 1. Definitions and Relationships A.
Separability of a Liquid Mixture B. Partial Pressures in Vapor
Mixtures C. Evaporation of Liquid Mixtures 2. Types of Mixtures A.
Ideal Binary Mixtures B. Nonideal Binary Mixtures C. Ideal
Multicomponent Mixtures D. Nonideal Multicomponent Mixtures III.
Continuous Rectifiers 1. Mode of Operations 2. Operating Lines A.
Enrichment Line B. The Stripping Line 3. Stepwise Separation in
Rectifiers A. Theoretical Plates for Separation of Binaries B. The
Reflux Ratio in the Separation of Binaries C. Multicomponent
Mixtures 4. Column Diameter and Column Throughput 5. Heat
Requirements IV. The Batch Still 1. Operation 2. Operating Line and
Separation Steps 3. Column Diameter, Column Throughput, and Heat
Requirements 4. Time for Separation and Related Variables at
Constant Product Concentration A. Molar Vapor Load Constant in Time
B. Heat Requirement Constant in Time 5. Separation Time for
Variable Heating Area V. The Semicontinuous Still 1. Operation 2.
Finding the Operating Lines, the Separation Steps, the Column Load,
the Column: Size, and the Heat Demand VI. Engineering Data,
Optimization of Costs, and Selection of Column Internals 1. General
A. Packing Types B. Plates and Trays 2. Designs and Functions A.
Packed Towers B. Plate Columns 3. Evaluation of Rectifying Columns
and Best Mode of Operation A. Evaluating and Calculations,
Separating Effect, Pressure Loss, Load, Specific Column Volume, and
Specific Column Cost B. Numerical Evaluation for Packed Towers C.
Quantitative Evaluation for Plate-Type Columns D. Packed Columns
versus Tray Columns-Operational Features and Cost E. Special
Designs for Vacuum Operation 4. Tests of Full-Size Tower Internals
VII. Optimum Separation 1. Optimization of Simple Columns A. The
Theory and Its Application B. Quantitative Evaluation 2.
Optimization of Multiple Columns A. Duplex Columns: Number of
Theoretical Steps, Reflux Ratios, and Vapor Loads B. Vapor Loads of
Multiple Columns Subdivided Because of Limited Height C. Optimizing
Duplex Rectifiers for Minimum Pressure Loss 3. Optimum Operation of
Combined Columns of Different Types Under Special Consideration A.
Parallel Arrangement B. Series Arrangement 4. Specialized
Operations A. Specialized Hookups and their Calculation B.
Rectification in Straight Stripping Columns C. Rectification in
Straight Enriching Columns D. Direct Heating of Columns E. Saving
Heat in Rectification VIII. Detail Planning of Separating Columns
1. General Viewpoints in the Selection of Column Types 2. Packed
Columns F. Maximum Loads for Metallic; Pall-Ring and Raschig Ring
Columns 3. Special Packings 4. Plate-Type Columns 5. Pressure
Losses in Rectification Columns IX. Partial Distillation 1.
Separation of Liquids by Continuous Partial Distillation 2.
Separation of Liquids by Discontinuous Partial Distillation X.
Partial Condensation 1. Partial Condensation in Dephlegmators 2.
Partial Countercurrent Direct Condensation in Columns XI.
Laboratory Columns and Pilot Plants 1. Distillation Columns with
Miniature Size Packing 2. Transferring Data Gained From
Semi-industrial Units to Full-Scale XII. Distillation in Fine and
High Vacuum 1. Molecular Distillation 2. Thin-Film Distillation 3.
Mechanism of Separation XIII. Components of a Separation Plant J.
Internal Components 2. Heat Exchangers 3. Pumps 4. Measuring and
Controls XIV. Use of Computers XV. Distillation and Environmental
Protection XVI. Outlook Bibliography Symbols and Units Glossary
Index
General
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