@article{scholars6984,
           pages = {13307--13317},
          volume = {57},
         journal = {Desalination and Water Treatment},
       publisher = {Taylor and Francis Inc.},
          number = {28},
            note = {cited By 7},
            year = {2016},
           title = {Phenol removal by newly isolated Acinetobacter baumannii strain Serdang 1 in a packed-bed column reactor},
             doi = {10.1080/19443994.2015.1063459},
        keywords = {bacterium; bioreactor; bioremediation; phenol; water treatment, Acinetobacter baumannii},
             url = {https://www.scopus.com/inward/record.uri?eid=2-s2.0-84936984769&doi=10.1080\%2f19443994.2015.1063459&partnerID=40&md5=2b73280a13e86a3be0ef8e7fbfe99ade},
          author = {Yadzir, Z. H. M. and Shukor, M. Y. and Ahmad, A. and Nazir, M. S. and Shah, S. M. U. and Abdullah, M. A.},
        abstract = {A 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{\^A} mg/L in 12{\^A} d at a rate of 6.04{\^A} 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{\^a}??77 phenol removal at the rate of 38.4{\^A} mg/L/h for 200{\^A} mg/L influent, which was almost three fold higher than the batch system. Low influent flow rate at 1.5{\^A} 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. {\^A}{\copyright} 2015 Balaban Desalination Publications. All rights reserved.},
            issn = {19443994}
}