Documents disponibles écrits par cet auteur

Kinetic study and scaleup of the oxidation of nanofiltration retentates by O3 / Steven Van Geluwe in Industrial & engineering chemistry research, Vol. 51 N° 20 (Mai 2012) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 51 N° 20 (Mai 2012) . - pp. 7056-7066 Titre : Kinetic study and scaleup of the oxidation of nanofiltration retentates by O3 Type de document : texte imprimé Auteurs : Steven Van Geluwe, Auteur ; Jan Degreve, Auteur ; Chris Vinckier, Auteur Année de publication : 2012 Article en page(s) : pp. 7056-7066 Note générale : Industrial chemistry Langues : Anglais (eng) Mots-clés : Membrane  separation  Nanofiltration  Oxidation  Kinetics Résumé : This paper reports on the upscaling of an O3 reactor for the oxidation of natural organic matter. Natural organic matter is responsible for fouling of nanofiltration membranes used for drinking water production. The proposed concept is to feed the retentate stream of a nanofiltration module (400 m3 h―1) to an O3 reactor (bubble column) and subsequently recycle it to a second nanofiltration module. The O3 oxidation of the retentate stream in the bubble column is analyzed in terms of the two-film theory with mass transfer and chemical reaction. The kinetic regime of the ozonation process, i.e., the chemical reaction rate relative to the mass-transfer rate, is determined using data from laboratory-scale experiments. This information is used for the calculation of the reactor volume and the required O3 dose on an industrial scale. An economic assessment of the integrated nanofiltration―O3 oxidation process also is given. ISSN : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=25925047 [article] Kinetic study and scaleup of the oxidation of nanofiltration retentates by O3 [texte imprimé] / Steven Van Geluwe, Auteur ; Jan Degreve, Auteur ; Chris Vinckier, Auteur . - 2012 . - pp. 7056-7066. Industrial chemistry Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 51 N° 20 (Mai 2012) . - pp. 7056-7066 Mots-clés : Membrane  separation  Nanofiltration  Oxidation  Kinetics Résumé : This paper reports on the upscaling of an O3 reactor for the oxidation of natural organic matter. Natural organic matter is responsible for fouling of nanofiltration membranes used for drinking water production. The proposed concept is to feed the retentate stream of a nanofiltration module (400 m3 h―1) to an O3 reactor (bubble column) and subsequently recycle it to a second nanofiltration module. The O3 oxidation of the retentate stream in the bubble column is analyzed in terms of the two-film theory with mass transfer and chemical reaction. The kinetic regime of the ozonation process, i.e., the chemical reaction rate relative to the mass-transfer rate, is determined using data from laboratory-scale experiments. This information is used for the calculation of the reactor volume and the required O3 dose on an industrial scale. An economic assessment of the integrated nanofiltration―O3 oxidation process also is given. ISSN : 0888-5885 En ligne : http://cat.inist.fr/?aModele=afficheN&cpsidt=25925047

Performance of solvent - pretreated polyimide nanofiltration membranes for separation of dissolved dyes from toluene / Siavash Darvishmanesh in Industrial & engineering chemistry research, Vol. 49 N° 19 (Octobre 2010) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 49 N° 19 (Octobre 2010) . - pp. 9330–9338 Titre : Performance of solvent - pretreated polyimide nanofiltration membranes for separation of dissolved dyes from toluene Type de document : texte imprimé Auteurs : Siavash Darvishmanesh, Auteur ; Jan Degreve, Auteur ; Bart Van der Bruggen, Auteur Année de publication : 2010 Article en page(s) : pp. 9330–9338 Note générale : Chimie industrielle Langues : Anglais (eng) Mots-clés : Solvent  Nanofiltration  Toluene Résumé : The major problem reported for commercially available membranes is their limited chemical stability in organic solvents. This article reports the influence of organic solvents with different polarity (methanol, acetone, acetic acid, toluene, and n-hexane) on the filtration performance of STARMEM membranes. These membranes are specified to be compatible with the solvents used. The pure toluene flux of these membranes and the rejection of azo dyes (Sudan Black and Rhodanile Blue) were measured before and after a week of exposure to one of the above-mentioned solvents. The results show that the structure of the membrane changed after pretreatment with polar solvents (methanol, acetone, acetic acid) and that the membrane performance shifts toward lower rejections with higher solvent flux. Nonpolar solvents do not change the polyimide membrane performances significantly. Contact angle measurements on new and solvent-treated membranes show that organic solvents change the hydrophobicity of polymeric membrane surfaces, leading to different toluene permeabilities before and after solvent treatment. Swelling measurements confirm the theory that a reorganization of the membrane material takes place, which leads to differences in porosity and changes in rejection. The study also shows that pretreatment of polyimide membranes with polar solvents increases the recovery of the membrane system when the solute size is large enough. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie101050k [article] Performance of solvent - pretreated polyimide nanofiltration membranes for separation of dissolved dyes from toluene [texte imprimé] / Siavash Darvishmanesh, Auteur ; Jan Degreve, Auteur ; Bart Van der Bruggen, Auteur . - 2010 . - pp. 9330–9338. Chimie industrielle Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 49 N° 19 (Octobre 2010) . - pp. 9330–9338 Mots-clés : Solvent  Nanofiltration  Toluene Résumé : The major problem reported for commercially available membranes is their limited chemical stability in organic solvents. This article reports the influence of organic solvents with different polarity (methanol, acetone, acetic acid, toluene, and n-hexane) on the filtration performance of STARMEM membranes. These membranes are specified to be compatible with the solvents used. The pure toluene flux of these membranes and the rejection of azo dyes (Sudan Black and Rhodanile Blue) were measured before and after a week of exposure to one of the above-mentioned solvents. The results show that the structure of the membrane changed after pretreatment with polar solvents (methanol, acetone, acetic acid) and that the membrane performance shifts toward lower rejections with higher solvent flux. Nonpolar solvents do not change the polyimide membrane performances significantly. Contact angle measurements on new and solvent-treated membranes show that organic solvents change the hydrophobicity of polymeric membrane surfaces, leading to different toluene permeabilities before and after solvent treatment. Swelling measurements confirm the theory that a reorganization of the membrane material takes place, which leads to differences in porosity and changes in rejection. The study also shows that pretreatment of polyimide membranes with polar solvents increases the recovery of the membrane system when the solute size is large enough. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie101050k