Efficiency of an up-flow Anaerobic Sludge Blanket reactor coupled with an electrochemical system to remove chloramphenicol in swine wastewater

The application and design of treatment systems in wastewater are necessary due to antibiotics' potential toxicity and resistant genes on residual effluent. This work evaluated a coupled bio-electrochemical system to reduce chloramphenicol (CAP) and chemical oxygen demand (COD) on swine wastewa...

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Veröffentlicht in:Water science and technology : a journal of the International Association on Water Pollution Research. - 1986. - 85(2022), 2 vom: 31. Jan., Seite 591-604
1. Verfasser: Romero-Soto, Itzel (VerfasserIn)
Weitere Verfasser: Garcia-Gomez, Celestino, Leyva-Soto, Luis, Napoles-Armenta, Juan, Concha-Guzman, María, Díaz-Tenorio, Lourdes, Ulloa-Mercado, Ruth, Drogui, Patrick, Buelna, Gerardo, Rentería-Mexia, Ana María, Gortáres-Moroyoqui, Pablo
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2022
Zugriff auf das übergeordnete Werk:Water science and technology : a journal of the International Association on Water Pollution Research
Schlagworte:Journal Article Sewage Waste Water Chloramphenicol 66974FR9Q1
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520 |a The application and design of treatment systems in wastewater are necessary due to antibiotics' potential toxicity and resistant genes on residual effluent. This work evaluated a coupled bio-electrochemical system to reduce chloramphenicol (CAP) and chemical oxygen demand (COD) on swine wastewater (SWW). SWW characterization found CAP of <10 μg/L and 17,434 mg/L of COD. The coupled system consisted of preliminary use of an Up-flow Anaerobic Sludge Blanket Reactor (UASB) followed by electrooxidation (EO). The UASB reactor (primary stage) was operated for three months at an organic load of 8.76 kg of COD/m3d and 50 mg CAP/L as initial concentration. In EO, we carried out a 22 (time operation and intensity) factorial design with a central composite design; we tried two Ti cathodes and one anode of Ti/PbO2. Optimal conditions obtained in the EO process were 240 min of operation time and 1.51 A of current intensity. It was possible to eliminate 44% of COD and 64.2% of CAP in the preliminary stage. On bio-electrochemicals, total COD and CAP removal were 82.35 and >99.99%, respectively. This coupled system can be applied to eliminate antibiotics and other organic pollutants in agricultural, industrial, municipal, and other wastewaters 
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700 1 |a Garcia-Gomez, Celestino  |e verfasserin  |4 aut 
700 1 |a Leyva-Soto, Luis  |e verfasserin  |4 aut 
700 1 |a Napoles-Armenta, Juan  |e verfasserin  |4 aut 
700 1 |a Concha-Guzman, María  |e verfasserin  |4 aut 
700 1 |a Díaz-Tenorio, Lourdes  |e verfasserin  |4 aut 
700 1 |a Ulloa-Mercado, Ruth  |e verfasserin  |4 aut 
700 1 |a Drogui, Patrick  |e verfasserin  |4 aut 
700 1 |a Buelna, Gerardo  |e verfasserin  |4 aut 
700 1 |a Rentería-Mexia, Ana María  |e verfasserin  |4 aut 
700 1 |a Gortáres-Moroyoqui, Pablo  |e verfasserin  |4 aut 
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