Distillation and Absorption 2006Eva Sørensen IChemE, 2006 - 1028 pages This work contains the proceedings of the Distillation and Absorption conference, which happens every 5 years. This collection of 100 contributions spanning 23 countries showcase the newest and best distillation and absorption technologies which cover a broad range of fundamental and applied aspects of the technology. To address these aspects, the contributions have been put into seven themes: modelling and simulation (steady-state, dynamic and CFD); energy efficiency and sustainability; equipment design and operation; integrated, hybrid and novel processes; process troubleshooting and handling operational problems; control and operation; and basic data. |
Table des matières
Plenary Lectures | 1 |
Challenges and Opportunities for the Suppliers | 21 |
The Dos and Donts of Distillation Column Control | 28 |
Industrial Absorption Current Status and Future | 44 |
Experimental Column Profile Maps with Varying | 111 |
Combining Shortcut Methods and Rigorous MINLP | 122 |
Energy Efficiency and Sustainability | 132 |
Biodiesel Production Lubricant Fractionating | 142 |
Its Measurement | 400 |
A New Method to Predict the Susceptibility to Form | 418 |
Basic Data | 431 |
New Method for the Determination of Batch | 440 |
Miniplant in Modelling Distillation for an Isooctene | 450 |
Control and Operation | 460 |
Design of Industrial Reactive Absorption Processes | 469 |
Basic Data | 498 |
Separation of MethanolButeneMTBE Using | 152 |
Thermal Integration of a Distillation Column | 162 |
Heat and Mass Transfer Characteristics of | 181 |
Modelling and Simulation | 190 |
A Nonlinear Wave Model with Variable | 200 |
Separation Performance of Structured Packed | 211 |
Prediction of Temperature and Concentration | 220 |
Equipment Design and Operation | 230 |
How to Surpass Conventional and High Capacity | 241 |
Liquid Distribution Behaviour of Conventional | 252 |
Modelling and Simulation | 273 |
A Modified Model of Computational Mass | 282 |
Equipment Design and Operation | 311 |
The Use of Directional Momentum Devices | 317 |
Distillation Trays that Operate Beyond | 327 |
Integrated Hybrid and Novel Processes | 336 |
Methyl Acetate Hydrolysis in a Reactive Divided | 353 |
Conceptual Design of Reactive Dividing Wall | 364 |
Experimental Investigation of Reactive Distillation | 373 |
Process Troubleshooting and Handling Operational Problems | 384 |
Foaming Effect on Random Packing Performance | 392 |
Solvent Properties of Functionalized Ionic Liquids | 511 |
Standardisation of Mass Transfer Measurements | 523 |
Integrated Hybrid and Novel Processes | 619 |
Optimal Configuration Design and Operation | 628 |
Stabilizing Operation of a 4Product Integrated | 638 |
Enrichment of Natural Products Using an Integrated | 648 |
Riser Design in Foam Fractionation | 657 |
P J Martin M Swain and R C Darton University | 666 |
Entrainer Selection for the Synthesis of Fatty Acid | 678 |
Pressure Swing Batch Distillation for Homogenous | 709 |
Study of the Thermally Coupled Distillation | 719 |
Dynamic Analysis of Distillation with Thermal | 728 |
Internal Columntocolumn Heat Transfer | 737 |
A Highefficiency Distillation System for Batch | 745 |
Modeling of Mixture Separation in a Column with | 764 |
The Sandwich Packing a New Type | 786 |
Equipment Design and Operation | 868 |
Modeling and Measurement of Macroscopic Flow | 1022 |
Shortcut Evaluation of Absorption for Synthesis | 1023 |
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Expressions et termes fréquents
absorption acetate acid AIChE amine azeotropic batch distillation binary bottom bubble calculated capacity Chem Chemical Engineering chemical equilibrium component composition concentration condenser configuration constant correlations diameter distillation column distillation processes distributor downcomer dynamic efficiency energy entrainer equation equilibrium stage experimental data experiments extractive distillation F-factor feed flow rate flowsheet heat transfer height HIDIC holdup interface ionic liquids layer liquid flow liquid load liquid phase maldistribution MDEA measured methanol method Methyl Acetate minimum mixture molar mole fraction MTBE multicomponent nonequilibrium number of stages obtained operation optimal optimisation orifice parameters performance pervaporation predicted pressure drop reaction reactive distillation reactor reboiler rectifying section reflux reflux ratio residue curve residue curve map separation shown in Figure simulation solution solvent stream stripping section structured packing surface Table Technology temperature thermally coupled thermodynamic total reflux trioxane values vapour variables velocity