Two-stage SBR for treatment of oil refinery wastewater

A two-stage sequencing batch reactor (SBR) system was used for treatment of oily wastewater with COD and oil and grease (O&G) concentrations ranging from 1,722-7,826 mg/L and 5,365-13,350 mg/L, respectively. A suitable start-up protocol was developed using gradual increase in oily wastewater com...

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Veröffentlicht in:Water science and technology : a journal of the International Association on Water Pollution Research. - 1986. - 50(2004), 10 vom: 07., Seite 243-9
1. Verfasser: Lee, L Y (VerfasserIn)
Weitere Verfasser: Hu, J Y, Ong, S L, Ng, W J, Ren, J H, Wong, S H
Format: Aufsatz
Sprache:English
Veröffentlicht: 2004
Zugriff auf das übergeordnete Werk:Water science and technology : a journal of the International Association on Water Pollution Research
Schlagworte:Journal Article Industrial Waste Petroleum Sewage Soil Pollutants Oxygen S88TT14065 Methanol Y4S76JWI15
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500 |a Date Revised 21.11.2013 
500 |a published: Print 
500 |a Citation Status MEDLINE 
520 |a A two-stage sequencing batch reactor (SBR) system was used for treatment of oily wastewater with COD and oil and grease (O&G) concentrations ranging from 1,722-7,826 mg/L and 5,365-13,350 mg/L, respectively. A suitable start-up protocol was developed using gradual increase in oily wastewater composition with methanol as the co-substrate. This strategy enabled a short acclimation period of 12 days for the sludge in the two-stage SBR to adapt to the oily wastewater. After acclimation, the 1st stage and 2nd stage SBRs were able to achieve COD removals of 47.0+/-2.4% and 95.3+/-0.5%, respectively. The 1st stage SBR was able to achieve 99.8+/-0.1% of O&G removal and effluent O&G from the 1st stage SBR was only 6+/-2 mg/L. The 2nd stage SBR was used to further remove COD in the effluent from the 1st stage SBR. The final effluent from the 2nd stage SBR had a COD concentration of 97+/-16 mg/L with no detectable O&G content. Thus, a two-stage SBR system was shown to be feasible for treating high strength oily wastewater to meet the local discharge standards 
650 4 |a Journal Article 
650 7 |a Industrial Waste  |2 NLM 
650 7 |a Petroleum  |2 NLM 
650 7 |a Sewage  |2 NLM 
650 7 |a Soil Pollutants  |2 NLM 
650 7 |a Oxygen  |2 NLM 
650 7 |a S88TT14065  |2 NLM 
650 7 |a Methanol  |2 NLM 
650 7 |a Y4S76JWI15  |2 NLM 
700 1 |a Hu, J Y  |e verfasserin  |4 aut 
700 1 |a Ong, S L  |e verfasserin  |4 aut 
700 1 |a Ng, W J  |e verfasserin  |4 aut 
700 1 |a Ren, J H  |e verfasserin  |4 aut 
700 1 |a Wong, S H  |e verfasserin  |4 aut 
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