Microbial degradation of phenol in a modified three-stage airlift packing-bed reactor

doi:10.2175/106143009X447885

CNU IR > College of Sustainable Environment and Recreation > Dept. of Environmental Engineering and Science (including master's program) > Periodical Articles > Item 310902800/25330

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题名:	Microbial degradation of phenol in a modified three-stage airlift packing-bed reactor
作者:	Huang, Cheng-Hsien Liou, Rey-May Chen, Shih-Hsiung Hung, Mu-Ya Lai, Cheng-Lee Lai, Juin-Yih
贡献者:	環境工程與科學系
关键词:	phenol hydraulic retention time modified three-stage airlift packing-bed bioreacto
日期:	2010-03
上传时间:	2012-05-31 09:57:43 (UTC+8)
摘要:	Phenol degradation was carried out by using a modified three-stage airlift packing-bed bioreactor. A laboratory-scale airlift packing-bed reactor, with hydrodynamic flexible packing material in the three-stage bioreactor, was constructed and operated for phenol removal from synthetic wastewater. The airlift packing-bed reactor successfully degraded phenol and lowered the chemical oxygen demand (COD) of wastewater. High COD removal was observed, and much lower sludge effluent was obtained in this investigation. This airlift bioreactor showed a superior hydrodynamics performance and broad operating conditions for phenolic material removal. Different operating modes were discussed to obtain the optimal condition for phenol degradation (i.e., hydraulic retention time [HRT] and gas flowrate of airlift). The HRT and feed phenol concentration of wastewater dominated the removal efficiency of phenol and COD. In this bioreactor, surface loading up to 2.84 g phenol/ m2 x d, almost 100% phenol removal, and over 90% COD removal was achieved. The lower operating cost combined with higher phenol-removal efficiency and a low sludge effluent concentration can be achieved by using this reactor for phenol wastewater treatment.
關聯:	water enviroment research 82(3)：p.249-258
显示于类别:	[Dept. of Environmental Engineering and Science (including master's program)] Periodical Articles

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