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- W4239555000 abstract "The electrochemical oxidation of phenol for waste water treatment applications was investigated on lead dioxide packedbed anodes. Cells were operated in both batch and continuous modes with feed streams up to 1100 mg/l phenol dissolved in aqueous solutions of Na2SO4 and H2SO4 or NaOH. All the phenol in solution could be readily oxidized but complete total organic carbon (T.O.C.) removal was more difficult. The percent phenol oxidized increased with increasing current density, and decreased as initial phenol concentration, electrolyte flow rate, pH and anode particle size were increased. Results are compared to simple mathematical models. On a étudié l'oxydation électrochimique du phénol, susceptible d'applications dans le traitement des eaux usées, sur une colonne garnie d'anodes de dioxyde de plomb. On a fait fonctionner ces cellulesc, d'une manière continue et d'une manière discontinue, en utilisant des courants d'alimentation contenant jusqu'à 1000 milligrammes par litre de phénol dissous dans des solutions aqueuses de Na2SO4 et H2SO4 ou NaOH. On a pu ainsi oxyder facilement tout le phénol en solution, mais il a été plus difficile d'enlever complètement tout le carbone organique (T.O.C.). I.c pourcentage du phénol oxydé s'est accru avec I'augmentation de la densité de courant et a diminué avec un accroissement de la concentration initiale du phénol, du débit de l'électrolyte et des dimensions des particules à l'anode. On a compare les résultats avec les prédictions de modèles mathématiques simples." @default.
- W4239555000 created "2022-05-12" @default.
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- W4239555000 date "1980-12-01" @default.
- W4239555000 modified "2023-09-27" @default.
- W4239555000 title "Anodic oxidation of phenol for waste water treatment" @default.
- W4239555000 cites W1984090757 @default.
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- W4239555000 doi "https://doi.org/10.1002/cjce.5450580607" @default.
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