Les Inscriptions à la Bibliothèque sont ouvertes en
ligne via le site: https://biblio.enp.edu.dz
Les Réinscriptions se font à :
• La Bibliothèque Annexe pour les étudiants en
2ème Année CPST
• La Bibliothèque Centrale pour les étudiants en Spécialités
A partir de cette page vous pouvez :
Retourner au premier écran avec les recherches... |
Détail de l'auteur
Auteur Atatürk Üniversitesi
Documents disponibles écrits par cet auteur
Affiner la rechercheElectrochemical mass transfer in impinging swirl jets / Atatürk Üniversitesi in Industrial & engineering chemistry research, Vol. 48 N°3 (Février 2009)
[article]
in Industrial & engineering chemistry research > Vol. 48 N°3 (Février 2009) . - p. 1593–1602
Titre : Electrochemical mass transfer in impinging swirl jets Type de document : texte imprimé Auteurs : Atatürk Üniversitesi, Auteur ; Mühendislik Fakültesi, Auteur ; Kimya Mühendisliği Bölümü, Auteur Année de publication : 2009 Article en page(s) : p. 1593–1602 Note générale : Chemical engineering Langues : Anglais (eng) Mots-clés : Electrochemical Jets -- Mass transfer Résumé :
The local mass transfer coefficients between an impinging swirl jet flow and a flat circular surface in a cylindrical cell were measured by the electrochemical limiting diffusion current technique. Helical-type swirl generators were used to generate swirl flow with intensities in the range of S = 0−0.73. The experiments were carried out for a jet Reynolds number range of 10 950−43 800, a nozzle-to-surface distance range of 2−10, and a dimensionless radial distance range of 0−15. The measured local mass transfer distributions in the radial direction exhibited an increase first and then a decrease and a converging behavior as the radial distance increased. It was observed that increasing Reynolds number increased the mass transfer rate, but its effect was reduced with an increase in swirl intensity. Increasing swirl intensity decreased transfer coefficients but increased their uniformity over the disk surface. The change in the nozzle-to-surface distance affected mass transfer coefficients up to a dimensionless radial distance of approximately r/dj < 8, and beyond this distance, they converged in almost one line, showing no effect of this parameter. Mass transfer correlations for Sherwood numbers whose average was taken over the surface and for Sherwood numbers at the stagnation point were developed as a function of the experimental parameters.En ligne : http://pubs.acs.org/doi/abs/10.1021/ie0715097 [article] Electrochemical mass transfer in impinging swirl jets [texte imprimé] / Atatürk Üniversitesi, Auteur ; Mühendislik Fakültesi, Auteur ; Kimya Mühendisliği Bölümü, Auteur . - 2009 . - p. 1593–1602.
Chemical engineering
Langues : Anglais (eng)
in Industrial & engineering chemistry research > Vol. 48 N°3 (Février 2009) . - p. 1593–1602
Mots-clés : Electrochemical Jets -- Mass transfer Résumé :
The local mass transfer coefficients between an impinging swirl jet flow and a flat circular surface in a cylindrical cell were measured by the electrochemical limiting diffusion current technique. Helical-type swirl generators were used to generate swirl flow with intensities in the range of S = 0−0.73. The experiments were carried out for a jet Reynolds number range of 10 950−43 800, a nozzle-to-surface distance range of 2−10, and a dimensionless radial distance range of 0−15. The measured local mass transfer distributions in the radial direction exhibited an increase first and then a decrease and a converging behavior as the radial distance increased. It was observed that increasing Reynolds number increased the mass transfer rate, but its effect was reduced with an increase in swirl intensity. Increasing swirl intensity decreased transfer coefficients but increased their uniformity over the disk surface. The change in the nozzle-to-surface distance affected mass transfer coefficients up to a dimensionless radial distance of approximately r/dj < 8, and beyond this distance, they converged in almost one line, showing no effect of this parameter. Mass transfer correlations for Sherwood numbers whose average was taken over the surface and for Sherwood numbers at the stagnation point were developed as a function of the experimental parameters.En ligne : http://pubs.acs.org/doi/abs/10.1021/ie0715097