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dc.contributor.authorYadzir, Z.H.M.-
dc.contributor.authorShukor, M.Y.-
dc.contributor.authorAhmad, A.-
dc.contributor.authorNazir, M.S.-
dc.contributor.authorShah, S.M.U.-
dc.contributor.authorAbdullah, M.A.-
dc.date.accessioned2017-04-09T05:12:19Z-
dc.date.available2017-04-09T05:12:19Z-
dc.date.issued2016-06-14-
dc.identifier.citationVol.57(28);13307-13317en_US
dc.identifier.urihttp://hdl.handle.net/123456789/5404-
dc.description.abstractA newly isolated Acinetobacter baumannii strain Serdang 1 was explored for its potential in phenol remediation in batch and continuous system. An immobilization cell system has been successfully developed to remove phenol in a batch system as high as 2,000 mg/L in 12 d at a rate of 6.04 mg/L/h. Repeated use of immobilized cells as many as five cycles was shown without any loss of activity. The continuous system in a packed-bed reactor achieved 65–77% phenol removal at the rate of 38.4 mg/L/h for 200 mg/L influent, which was almost three fold higher than the batch system. Low influent flow rate at 1.5 mL/min and bed height-to-diameter ratio of 15.2 reached steady state faster than the higher flow rate, and the percentage of phenol removal was also higher.en_US
dc.language.isoenen_US
dc.publisherDesalination and Water Treatmenten_US
dc.titlePhenol Removal By Newly Isolated Acinetobacter Baumannii Strain Serdang 1 In A Packed-Bed Column Reactoren_US
dc.typeArticleen_US
Appears in Collections:Journal Articles

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