Page 6 - Applied Process Design For Chemical And Petrochemical Plants Volume II

Contents

Preface to Third Edition ............................ V 63; Unequal Molal Flow, 63; Ponchon-Savant Method, 63;
Example 8-21: Ponchon Unequal Molal Overflow, 65; Mul-
ticomponent Dwtillation, 68; Minimum Reflux Ratio -
8. Distillation .............................................. 1 Infinite Plates, 68; Example 8-22: Multicomponent Distilla-
tion by Yaw’s Method, 70; Algebraic Plateto-Plate Method,
70; Underwood Algebraic Method, 71; Example 8-23: Min-
Part 1 imum Reflux Ratio Using Underwood Equation, 73; Mini-
Distillation Process Performance .................... 1 mum Reflux Colburn Method, 74; Example 8-24 Using
the Colburn Equation to Calculate Minimum Reflux Ratio,
Equilibrium Basic Consideration, 1; Ideal Systems, 2; IG 76; Scheibel-Montross Empirical: Adjacent Key Systems,
Factor Hydrocarbon Equilibrium Charts, 4; Non-Ideal Sys- 79; Example 825: Scheibel-Montross Minimum Reflux, 80;
tems, 5; Example 8-1: Raoult’s Law, 14; Binary System Minimum Number of Trays: Total Reflux - Constant
Material Balance: Constant Molal Overflow Tray to Tray, Volatility, 80; Chou and Yaws Method, 81; Example 8-26:
18; Example 8-2: Bubble Point and Dew Point, 17; Exam- Distillation with Two Sidestream Feeds, 82; Theoretical
ple 8-3: Flashing Composition; Distillation Operating hs- Trays at Operating Reflux, 83; Example 8-27 Operating
sures, 18; Total Condenser, 19; Partial Condenser, 20; Reflux Ratio, 84; Estimating Multicomponent Recoveries,
Thermal Condition of Feed, 20; Total Reflux, Minimum 85; Example 8-28: Estimated Multicomponent Recoveries
Plates, 21; Fenske Equation: Overall Minimum Total Tray by Yaw’s Method, 87; Tray-by-Tray Using a Computer, 90;
with Total Condenser, 22; Relative Volatility, 22; Example 8- Example 8-29: Tray-to-Tray Design Multicomponent
4 Determine Minimum Number of Trays by Winn’s Mixture, 90; Example 8-30: Tray-by-Tray Multicomponent
Method, 24; Example 8-5: Boiling Point Curve and Equi- Mixture Using a Computer, 95; Computer Printout for
librium Diagram for Benzene-Toluene Mixture, 26; Exam- Multicomponent Distillation, 95; Example 8-31: Multi-
ple 8-7: Flash Vaporization of a Hydrocarbon Liquid Mix- component Examination of Reflux Ratio and Distillate to
ture, 27; Quick Estimate of Relative Volatility, 28; Example Feed Ratio, 99; Example 8-32: Stripping Dissolved Organ-
8-8: Relative Volatility Estimate by Wagle’s Method, 29; ics from Water in a Packed Tower Using Method of Li and
Minimum Reflux Ratio: Infinite Plates, 29; Theoretical Hsiao, 100; Troubleshooting, Predictive Maintenance, and
Trays at Actual Reflux, 30; Example 8-9: Solving Gilliland’s Controls for Distillation Columns, 101; Nomenclature for
Equation for Determining Minimum Theoretical Plates for Part 1,102
Setting Actual Reflux, 32; “Pinch Conditions” on x-y Dia-
gram at High Pressure, 32; Example 8-10: Graphical
Design for Binary Systems, 33; Example 8-11: Thermal Part 2
Condition of Feed, 35; Example 8-12: Minimum Theoreti- Hydrocarbon Absorption
cal Trays/Plates/Stages at Total Reflux, 38; Tray Eficiency, and Stripping .................................................... 108
40; Example 8-13: Estimating Distillation Tray Efficiency,
42; Batch Distillation, 45; Differential Distillation, 46; Sim- Kremser-Brown-Shenvood Method - No Heat of Absorp
ple Batch Distillation, 47; Fixed Number Theoretical Trays, tion, 108; Absorption - Determine Component Absorp-
48; Batch with Constant Reflux Ratio, 48; Batch with Vari- tion in Fixed Tray Tower, 108; Absorption - Determine
able Reflux Rate Rectification, 50; Example 8-14 Batch Number of Trays for Specified Product Absorption, 109;
Distillation, Constant Reflux; Following the Procedure of Stripping - Determine Theoretical Trays and Stripping or
Block, 51; Example 8-18: Vapor Boil-up Rate for Fixed Gas Rate for a Component Recovery, 110; Stripping -
Trays, 53; Example 8-16: Binary Batch Differential Distilla- Determine Stripping-Medium Rate for Fixed Recovery,
tion, 54; Example 8-17: Multicomponent Batch Distilla- 11 1; Absorption - Edmister Method, 112; Example 8-33:
tion, 53; Steam Distillation, 57; Example 8-18: Multicom- Absorption of Hydrocarbons with Lean Oil, 114; Inter-
ponent Steam Flash, 59; Example 8- 18: Continuous Steam cooling for Absorbers, 116; Absorption and Stripping Effi-
Flash Separation Process - Separation of Non-Volatile ciency, 118; Example 8-34 Determine Number of Trays for
Component from Organics, 61; Example 8-20: Open Specified Product Absorption, 118; Example 8-35: Deter-
Steam Stripping of Heavy Absorber Rich Oil of Light mine Component Absorption in Fixed-Tray Tower, 119;
Hydrocarbon Content, 62; Distillation with Heat Balance, Nomenclature for Part 2, 121