Application of equilibrium theory to ternary moving bed configurations (four+four, five+four, eight and nine zones)
Identifieur interne : 000507 ( Istex/Checkpoint ); précédent : 000506; suivant : 000508Application of equilibrium theory to ternary moving bed configurations (four+four, five+four, eight and nine zones)
Auteurs : Alexandre Nicolaos [France] ; Laurence Muhr [France] ; Patrice Gotteland [France] ; Roger-Marc Nicoud [France] ; Michel Bailly [France]Source :
- Journal of Chromatography A [ 0021-9673 ] ; 2001.
English descriptors
- KwdEn :
- Adsorption, Adsorption isotherms, Axial dispersion, Binary mixture, Case feed, Chemical compounds, Chromatogr, Chromatographic column, Chromatographic columns, Compound, Concentration step, Cost function, Different devices, Different objective functions, Elsevier science, Eluent, Eluent compound, Entire process, Equilibrium theory, Flow rate ratio, Four1four zone, French patent, General hypotheses, Goal function, Highest value, Internal recycling, Isotherm, Kinetic resistance, Linear adsorption isotherm, Linear adsorption isotherms, Liquid phase, Mass balance equation, Maximum pressure drop constraint, Migration direction, Migration direction rules, Migration directions, Morbidelli, Multicomponent mixture, Nicolaos, Nicoud, Outlet streams, Performance comparison, Point rule, Point rules, Practical considerations, Pure compound, Pure compounds, Pure fractions, Pure products, Retention parameters, Same methodology, Single device, Solid phase, Solvent consumption, Solvent consumption point, Stationary phase, Steady state, Target compound, Ternary, Ternary mixture, Tmbs, Total eluent, Ve1four, Ve1four zone, Work frame, Zone, Zone migration direction, Zone tmbs, Zones1four zones.
- Teeft :
- Adsorption, Adsorption isotherms, Axial dispersion, Binary mixture, Case feed, Chemical compounds, Chromatogr, Chromatographic column, Chromatographic columns, Compound, Concentration step, Cost function, Different devices, Different objective functions, Elsevier science, Eluent, Eluent compound, Entire process, Equilibrium theory, Flow rate ratio, Four1four zone, French patent, General hypotheses, Goal function, Highest value, Internal recycling, Isotherm, Kinetic resistance, Linear adsorption isotherm, Linear adsorption isotherms, Liquid phase, Mass balance equation, Maximum pressure drop constraint, Migration direction, Migration direction rules, Migration directions, Morbidelli, Multicomponent mixture, Nicolaos, Nicoud, Outlet streams, Performance comparison, Point rule, Point rules, Practical considerations, Pure compound, Pure compounds, Pure fractions, Pure products, Retention parameters, Same methodology, Single device, Solid phase, Solvent consumption, Solvent consumption point, Stationary phase, Steady state, Target compound, Ternary, Ternary mixture, Tmbs, Total eluent, Ve1four, Ve1four zone, Work frame, Zone, Zone migration direction, Zone tmbs, Zones1four zones.
Abstract
Abstract: In this article, different ternary moving bed configurations are studied by determining the working flow-rates of the equivalent true moving bed at the low solvent consumption point using equilibrium theory. This method has been applied for linear adsorption isotherms. The simulated moving bed flow-rates can then be calculated and a final comparison between the performances of each process is given based upon two different objective functions.
Url:
DOI: 10.1016/S0021-9673(00)00937-7
Affiliations:
- France
- Auvergne-Rhône-Alpes, Grand Est, Lorraine (région), Rhône-Alpes
- Décines-Charpieu, Nancy, Vandoeuvre-lès-Nancy
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<author><name sortKey="Gotteland, Patrice" sort="Gotteland, Patrice" uniqKey="Gotteland P" first="Patrice" last="Gotteland">Patrice Gotteland</name>
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<term>Case feed</term>
<term>Chemical compounds</term>
<term>Chromatogr</term>
<term>Chromatographic column</term>
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<term>Different devices</term>
<term>Different objective functions</term>
<term>Elsevier science</term>
<term>Eluent</term>
<term>Eluent compound</term>
<term>Entire process</term>
<term>Equilibrium theory</term>
<term>Flow rate ratio</term>
<term>Four1four zone</term>
<term>French patent</term>
<term>General hypotheses</term>
<term>Goal function</term>
<term>Highest value</term>
<term>Internal recycling</term>
<term>Isotherm</term>
<term>Kinetic resistance</term>
<term>Linear adsorption isotherm</term>
<term>Linear adsorption isotherms</term>
<term>Liquid phase</term>
<term>Mass balance equation</term>
<term>Maximum pressure drop constraint</term>
<term>Migration direction</term>
<term>Migration direction rules</term>
<term>Migration directions</term>
<term>Morbidelli</term>
<term>Multicomponent mixture</term>
<term>Nicolaos</term>
<term>Nicoud</term>
<term>Outlet streams</term>
<term>Performance comparison</term>
<term>Point rule</term>
<term>Point rules</term>
<term>Practical considerations</term>
<term>Pure compound</term>
<term>Pure compounds</term>
<term>Pure fractions</term>
<term>Pure products</term>
<term>Retention parameters</term>
<term>Same methodology</term>
<term>Single device</term>
<term>Solid phase</term>
<term>Solvent consumption</term>
<term>Solvent consumption point</term>
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<term>Steady state</term>
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<term>Ternary</term>
<term>Ternary mixture</term>
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<term>Total eluent</term>
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<term>Ve1four zone</term>
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<term>Chromatogr</term>
<term>Chromatographic column</term>
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<term>Cost function</term>
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<term>Different objective functions</term>
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<term>Eluent compound</term>
<term>Entire process</term>
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<term>French patent</term>
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<term>Point rules</term>
<term>Practical considerations</term>
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<term>Pure compounds</term>
<term>Pure fractions</term>
<term>Pure products</term>
<term>Retention parameters</term>
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<term>Single device</term>
<term>Solid phase</term>
<term>Solvent consumption</term>
<term>Solvent consumption point</term>
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<term>Steady state</term>
<term>Target compound</term>
<term>Ternary</term>
<term>Ternary mixture</term>
<term>Tmbs</term>
<term>Total eluent</term>
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<front><div type="abstract" xml:lang="en">Abstract: In this article, different ternary moving bed configurations are studied by determining the working flow-rates of the equivalent true moving bed at the low solvent consumption point using equilibrium theory. This method has been applied for linear adsorption isotherms. The simulated moving bed flow-rates can then be calculated and a final comparison between the performances of each process is given based upon two different objective functions.</div>
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