[article]
Titre : |
Enhancement of gas-to-water mass-transfer rates by the second liquid phase |
Type de document : |
texte imprimé |
Auteurs : |
Zhigang Zhang, Auteur ; Wei Chen, Auteur ; Sansan Yu, Auteur |
Année de publication : |
2010 |
Article en page(s) : |
pp. 3223–3227 |
Note générale : |
Industrial Chemistry |
Langues : |
Anglais (eng) |
Mots-clés : |
Gas Water Mass Rates Liquid |
Résumé : |
Gas−liquid mass-transfer enhancement due to the presence of a second dispersed liquid phase has been discussed in this paper. Both the overall volumetric mass-transfer coefficient from the gas to bulk liquid and the partition coefficient were calculated under non-steady-state conditions. The results showed that the enhancement factor increased with an increase of the partition coefficient and the volumetric mass-transfer coefficient KLa clearly increased when a second dispersed liquid phase was added, with a clear maximum at 3% of the dispersed-phase volume fraction. The influence of the dispersed phase on KLa markedly depended on the agitation rate, and a maximum KLa was attained between 650 and 700 rpm. |
ISSN : |
0888-5885 |
En ligne : |
pp. 3223–3227 |
in Industrial & engineering chemistry research > Vol. 49 N° 7 (Avril 2010) . - pp. 3223–3227
[article] Enhancement of gas-to-water mass-transfer rates by the second liquid phase [texte imprimé] / Zhigang Zhang, Auteur ; Wei Chen, Auteur ; Sansan Yu, Auteur . - 2010 . - pp. 3223–3227. Industrial Chemistry Langues : Anglais ( eng) in Industrial & engineering chemistry research > Vol. 49 N° 7 (Avril 2010) . - pp. 3223–3227
Mots-clés : |
Gas Water Mass Rates Liquid |
Résumé : |
Gas−liquid mass-transfer enhancement due to the presence of a second dispersed liquid phase has been discussed in this paper. Both the overall volumetric mass-transfer coefficient from the gas to bulk liquid and the partition coefficient were calculated under non-steady-state conditions. The results showed that the enhancement factor increased with an increase of the partition coefficient and the volumetric mass-transfer coefficient KLa clearly increased when a second dispersed liquid phase was added, with a clear maximum at 3% of the dispersed-phase volume fraction. The influence of the dispersed phase on KLa markedly depended on the agitation rate, and a maximum KLa was attained between 650 and 700 rpm. |
ISSN : |
0888-5885 |
En ligne : |
pp. 3223–3227 |
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