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Adsorption of volatile organic compounds. experimental and theoretical study / Cristian C. Brunchi in Industrial & engineering chemistry research, Vol. 51 N° 51 (Décembre 2012) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 51 N° 51 (Décembre 2012) . - pp. 1029-1038 Titre : Adsorption of volatile organic compounds. experimental and theoretical study Type de document : texte imprimé Auteurs : Cristian C. Brunchi, Auteur ; Juan Manuel Castillo Sanchez, Auteur ; Andrzej I. Stankiewicz, Auteur Année de publication : 2012 Article en page(s) : pp. 1029-1038 Note générale : Industrial chemistry Langues : Anglais (eng) Mots-clés : Flue  gas  purification  Physicochemical  purification  Gas  solid  adsorption  Fixed  bed  Inorganic  adsorbent  Activated  carbon  Granular  material  Organic  adsorbate  Ternary  mixture Résumé : A simple mathematical model has been developed to simulate multicomponent fixed bed adsorption. The Linear Driving Force model is used to describe the intraparticle mass transfer. The competitive effect is accounted for through the multicomponent adsorption isotherm. This multicomponent equilibrium is described by the Ideal Adsorbed Solution Theory (IAST). To apply this theory, pure component adsorption isotherm data are represented by the Freundlich equation on a piecewise basis. For the prediction, operating conditions (flow rates, bed depths, input concentrations) and some characteristics of activated carbon must be known. It is also necessary to have pure component isotherm data. To demonstrate the applicability of the model, fixed bed experiments were carried out using a ternary mixture, containing methylethylketone, ethylene chloride, methylene chloride. A good agreement between calculations and experiments was obtained. ISSN : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=2417229 [article] Adsorption of volatile organic compounds. experimental and theoretical study [texte imprimé] / Cristian C. Brunchi, Auteur ; Juan Manuel Castillo Sanchez, Auteur ; Andrzej I. Stankiewicz, Auteur . - 2012 . - pp. 1029-1038. Industrial chemistry Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 51 N° 51 (Décembre 2012) . - pp. 1029-1038 Mots-clés : Flue  gas  purification  Physicochemical  purification  Gas  solid  adsorption  Fixed  bed  Inorganic  adsorbent  Activated  carbon  Granular  material  Organic  adsorbate  Ternary  mixture Résumé : A simple mathematical model has been developed to simulate multicomponent fixed bed adsorption. The Linear Driving Force model is used to describe the intraparticle mass transfer. The competitive effect is accounted for through the multicomponent adsorption isotherm. This multicomponent equilibrium is described by the Ideal Adsorbed Solution Theory (IAST). To apply this theory, pure component adsorption isotherm data are represented by the Freundlich equation on a piecewise basis. For the prediction, operating conditions (flow rates, bed depths, input concentrations) and some characteristics of activated carbon must be known. It is also necessary to have pure component isotherm data. To demonstrate the applicability of the model, fixed bed experiments were carried out using a ternary mixture, containing methylethylketone, ethylene chloride, methylene chloride. A good agreement between calculations and experiments was obtained. ISSN : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=2417229