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NAMS 2002 Workshop - ICOM 2008

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Drinking and Wastewater Applications V – 2<br />

Friday July 18, 3:00 PM-3:30 PM, Maui<br />

Treatment Performance and Detoxification of Coke Plant Wastewater Using<br />

an Anaerobic-Anoxic-Oxic Membrane Bioreactor System<br />

W. Zhao (Speaker), Div. of Water Environment, Dept, of Environmental Science and Engineering,<br />

China - xhuang@tsinghua.edu.cn<br />

X. Huang, Div. of Water Environment, Dept, of Environmental Science and Engineering, China<br />

D. Lee, Chemical Engineering Department, National Taiwan University, Taiwan<br />

M. He, Div. of Water Environment, Dept, of Environmental Science and Engineering, China<br />

Coke plant wastewater is a kind of complex industrial wastewater generated in<br />

the iron and steel industry during coal carbonization and fuel classification. Its<br />

quantity and quality may vary fairly widely, depending on coal quality, coking<br />

temperature, and by-product recovery processes. The major contaminants in a<br />

typical coke plant wastewater consist of high concentration ammonia, toxic<br />

substances (such as cyanide, thiocyanate, phenols), and biologically inhibitory<br />

organic compounds. The conventional activated sludge process is usually not<br />

potent enough for removal and detoxification of these pollutants. Due to<br />

increasingly stringent regulations for receiving water bodies and industrial<br />

wastewater reuse strategies, achieving effective and safe control of this kind of<br />

wastewater is imperative. In this study, an anaerobic-anoxic-oxic membrane<br />

bioreactor (MBR) system was proposed to treat coke plant wastewater.<br />

Treatment performance at different hydraulic retention times (HRTs) was<br />

investigated. Acute toxicity test was applied to evaluate the toxicity change<br />

during the MBR system, and transformation of organic pollutants in the system<br />

was also analyzed.<br />

The MBR system consisted of an anaerobic reactor (A1), an anoxic reactor (A2)<br />

and an oxic reactor (O) with a submerged hollow fibre polythene membrane<br />

(nominal pore size: 0.4 μm, membrane area: 0.2 m 2 , Mitsubishi, Japan). The<br />

anaerobic reactor was packed with soft media. The anoxic and oxic reactors<br />

were completely mixed tanks, and the mixed liquor recirculation was from the<br />

oxic one to the anoxic one. Compared conventional anaerobic-anoxic-oxic<br />

activated (CAS) system was operated at the same condition with MBR system.<br />

Raw coke plant wastewater was collected from Beijing Steel Company. Acute<br />

toxicity of wastewater was assessed by luminescent bacteria growth inhibition<br />

test, using Zn 2+ as the toxicity reference substance. Transformation of organic<br />

pollutants in the system was analyzed by fluorescence excitation- emission<br />

matrix (EEM). The MBR process was operated in a constant mode. When the<br />

transmembrane pressure (TMP) reached around 0.3MPa, off line physical (with<br />

tap water) and chemical (with HCl, NaOH, NaClO) cleaning of the membrane

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