| Literature DB >> 26894292 |
Changyong Wu1, Yuexi Zhou2, Qingliang Sun3, Liya Fu4, Hongbo Xi1, Yin Yu1, Ruozhen Yu5.
Abstract
A hydrolysis acidification (HA)-anoxic-oxic (A/O) process was adopted to treat a petrochemical wastewater. The operation optimization was carried out firstly by a bench scale experimental reactor. Then a full scale petrochemical wastewater treatment plant (PCWWTP, 6500 m(3) h(-1)) was operated with the same parameters. The results showed that the BOD5/COD of the wastewater increased from 0.30 to 0.43 by HA. The effluent COD was 54.4 mg L(-1) for bench scale reactor and 60.9 mg L(-1) for PCWWTP when the influent COD was about 480 mg L(-1) on optimized conditions. The organics measured by gas chromatography-mass spectrometry (GC-MS) reduced obviously and the total concentration of the 5 organics (1,3-dioxolane, 2-pentanone, ethylbenzene, 2-chloromethyl-1,3-dioxolane and indene) detected in the effluent was only 0.24 mg L(-1). There was no obvious toxicity of the effluent. However, low acute toxicity of the effluent could be detected by the luminescent bacteria assay, indicating the advanced treatment is needed. The clone library profiling analysis showed that the dominant bacteria in the system were Acidobacteria, Proteobacteria and Bacteriodetes. HA-A/O process is suitable for the petrochemical wastewater treatment.Entities:
Keywords: Biodegradability; Clone library; Organic pollutants removal; Petrochemical wastewater; Wastewater toxicity
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Year: 2016 PMID: 26894292 DOI: 10.1016/j.jhazmat.2016.02.007
Source DB: PubMed Journal: J Hazard Mater ISSN: 0304-3894 Impact factor: 10.588