Distillation Fundamentals and Principles Handbooks in Separation Science Series
Coordonnateurs : Gorak Andrzej, Sorensen Eva
1. History of Distillation 2. Vapour-Liquid Equilibrium and Physical Properties for Distillation 3. Mass Transfer in Distillation 4. Principles of Binary Distillation 5. Design and Operation of Batch Distillation 6. Energy Considerations in Distillation 7. Conceptual Design of Zeotropic Distillation Processes 8. Conceptual Design of Azeotropic Distillation Processes 9. Conceptual Design of Hybrid Distillation Processes 10. Modelling of Distillation Processes 11. Optimisation of Distillation Processes
practitioners of distillation and separation science, looking for a quick access to the newest knowledge, graduate students searching for special applications, chemist, environmental engineers, mechanical engineers.
70% professionals, 20% students, 10% others.
Dr. Eva Sørensen is a Reader in Chemical Engineering at University College London. She has worked within the area of fluid separations for over 20 years, and has extensive experience in academic research and in teaching. Dr. Sørensen is a Chartered Engineer, a Chartered Scientist, a Fellow of the Institution of Chemical Engineers (IChemE), and a Fellow of the Higher Education Academy (HEA).
- Winner of the 2015 PROSE Award in Chemistry & Physics from the Association of American Publishers
- Practical information on the newest development written by recognized experts
- Coverage of a huge range of laboratory and industrial distillation approaches
- Extensive references for each chapter facilitates further study
Date de parution : 07-2014
Ouvrage de 450 p.
19x23.3 cm
Thèmes de Distillation :
Mots-clés :
Alcohol distillation; Azeotropic behavior; Azeotropic distillation; Batch; Binary; Coal tar refining; Column efficiency; Conceptual design; Configuration; Control; Cryogenic air separation; Curved-boundary distillation; Detailed design; Differential distillation; Distillation; Distillation configurations; Distillation design; Distillation sequencing; Distillation trains; Dortmund Data Bank; Double-effect distillation (two-pressure distillation); Energy efficiency; Energy efficient distillation; Energy optimization; Entrainer selection; Equations of state; Extractive; Extractive distillation; Fenske-Underwood-Gilliland; Film model; Finite reflux; Flash distillation; Fractionation; Group contribution methods; Heat integration; Heat pumping (compression refrigeration; vapor recompression); Heat transfer; Heating and cooling duties; Heteroazeotropic distillation; Hydrodynamic analogies; Innovation; Innovation cycle; Integrated process steps; Intermediate heating and cooling (side-reboiler; side-condenser); Internal heat integrated column; Inverted; Mass production; Mass transfer; Matrix method; McCabe-Thiele; Middle vessel; Modeling; Multi vessel; Multicomponent distillation; Offcut; Operation; Optimization; Petroleum distillation; Pinch distillation boundary; Prefractionation (dividing wall column); Pressure-swing; Pressure-swing distillation; Process intensification; Rate-based approach; Rayleigh; Reactive; Rectification; Shortcut methods; Simple distillation boundary; Split feasibility; Structured packing; Thermal coupling (side-stripper; side-rectifier); Thermophysical properties; Total reflux and reversible distillation; Total reflux distillation boundary; Tray development; Underwood's equation; Vapor-liquid equilibrium; gE-models