Organic semiconductor wastewater treatment using a four-stage Bardenpho with membrane system

Electronic wastewater from a semiconductor plant was treated with a pilot-scale four-stage Bardenpho process with membrane system. The system was operated over a 14-month period with an overall hydraulic retention time (HRT) ranging from 9.5 to 30 h. With a few exceptions, the pilot plant consistent...

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Veröffentlicht in:Environmental technology. - 1998. - 35(2014), 21-24 vom: 30. Nov., Seite 2837-45
1. Verfasser: Chung, Jinwook (VerfasserIn)
Weitere Verfasser: Fleege, Daniel, Ong, Say Kee, Lee, Yong-Woo
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2014
Zugriff auf das übergeordnete Werk:Environmental technology
Schlagworte:Journal Article four-stage Bardenpho hydraulic retention time membrane semiconductor specific denitrification rate Industrial Waste Membranes, Artificial Waste Water Water Pollutants, Chemical mehr... Nitrogen N762921K75
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520 |a Electronic wastewater from a semiconductor plant was treated with a pilot-scale four-stage Bardenpho process with membrane system. The system was operated over a 14-month period with an overall hydraulic retention time (HRT) ranging from 9.5 to 30 h. With a few exceptions, the pilot plant consistently treated the electronic wastewater with an average removal efficiency of chemical oxygen demand (COD) and total nitrogen of 97% and 93%, respectively, and achieving effluent quality of COD<15 mg/L, turbidity<1, and silt density index<1. Based on removal efficiencies of the pilot plant, it is possible to lower the HRT to less than 9.5 h to achieve comparable removal efficiencies. An energy-saving configuration where an internal recycle line was omitted and the biomass recycle was rerouted to the pre-anoxic tank, can reduce energy consumption by 8.6% and gave removal efficiencies that were similar to the Bardenpho process. The system achieved pre-anoxic and post-anoxic specific denitrification rate values with a 95% confidence interval of 0.091 ± 0.011 g NO₃-N/g MLVSS d and 0.087 ± 0.016 g NO₃-N/g MLVSS d, respectively. The effluent from the four-stage Bardenpho with membrane system can be paired with a reverse osmosis system to provide further treatment for reuse purposes 
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700 1 |a Fleege, Daniel  |e verfasserin  |4 aut 
700 1 |a Ong, Say Kee  |e verfasserin  |4 aut 
700 1 |a Lee, Yong-Woo  |e verfasserin  |4 aut 
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