Ludwig's Applied Process Design for Chemical and Petrochemical Plants: Volume 2: Distillation, packed towers, petroleum fractionation, gas processing and dehydration, Volume 2The Fourth Edition of Applied Process Design for Chemical and Petrochemical Plants Volume 2 builds upon the late Ernest E. Ludwig’s classic chemical engineering process design manual. Volume Two focuses on distillation and packed towers, and presents the methods and fundamentals of plant design along with supplemental mechanical and related data, nomographs, data charts and heuristics. The Fourth Edition is significantly expanded and updated, with new topics that ensure readers can analyze problems and find practical design methods and solutions to accomplish their process design objectives.
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Contents
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Chapter 11 Petroleum ComplexMixture Fractionation Gas Processing Dehydration Hydrocarbon Absorption and Stripping | 269 |
Chapter 12 Enhanced distillation types | 345 |
Mechanical Designs fornbspTray Performance | 373 |
Chapter 14 Packed Towers | 483 |
References for Chapters 10 1112 and 13 | 679 |
References for Chapter 14 | 687 |
Bibliography | 691 |
Appendix D Alphabetical Conversion Factors | 793 |
Appendix E Equations and Analysis | 871 |
Appendix F Solving Equations Using Excel | 885 |
Appendix G Analytical Techniques | 895 |
Appendix H Numerical Techniques | 901 |
Appendix I Screenshot Guide to Absoft Compiler Graphical User Interface | 917 |
Appendix J Equilibrium KValues | 925 |
Appendix K Simulations | 939 |
Other editions - View all
Ludwig's Applied Process Design for Chemical and Petrochemical Plants A. Kayode Coker No preview available - 2007 |
Ludwig's Applied Process Design for Chemical and Petrochemical Plants ... A. Kayode Coker No preview available - 2010 |
Common terms and phrases
absorption acetate acid azeotrope batch distillation boiling point bottoms bubble cap bubble point calculated capacity Carbon Chem Chemical Engineers coefficient composition condenser constant correlation Cubic curve density determine diagram distillation column downcomer efficiency enthalpy entrainment Equation equilibrium factor feed flooding flow rate ft/sec ft² heat heavy key height HETP holes Hydrocarbon inches inlet Intalox key component light key liquid flow liquid phase liquid rate methanol method Methyl methyl acetate mixture Mole fraction mols/hr Multicomponent number of theoretical Nutter operating line overhead packed tower performance permission pressure drop Process Flow Diagrams Prog psia Raschig rings reactive distillation reboiler relative volatility rights reserved sieve trays slot solution stream structured packing Table temperature theoretical plates theoretical trays tower diameter transfer units tray spacing values valve trays vapor pressure vapor rate viscosity weir