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Integrated Method of Ozonation and Anaerobic Process for Treatment of Atrazine bearing Wastewater
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The paper presents the treatment of atrazine-contaminated wastewater by ozonation followed by an anaerobic process using Upflow Anaerobic Sludge Blanket (UASB) reactor. The experiment was performed with 100 ppb synthetic solutions of atrazine prepared in ultra-pure water. The corresponding initial Chemical Oxygen Demand (COD) is 226 mg.L-1. The initial pH was adjusted to 9.5. The atrazine-bearing synthetic wastewater was ozonated with an ozone dose of 9.4mg/l for 40 minutes of optimum ozonation time, resulting in a 35% reduction in the initial concentration of atrazine. Along with atrazine reduction, there was a COD removal of 54.42%. Further, it was degraded with an anaerobic process, resulting in the final reduction in atrazine concentration of 81% and the corresponding removal in COD of 86.7%. The process of ozonation led to the mineralization of atrazine and enhancement in the biodegradability of the wastewater. Using ion chromatography, the ozonated wastewater sample was analyzed for ionic by-products before and after ozonation. The ion chromatography results showed the breaking of the atrazine compound and the formation of Cl-, NO3-, SO42-, and F- as intermediate products. Further, the BOD5/COD ratio increased, reflecting the increased biodegradability. This ozonated wastewater was treated in a UASB reactor where the pesticide was degraded to 19 ppb, and COs degraded to 30 mg.L-1. The overall removal of atrazine pesticide and COD were 81% and 86.7%, respectively, in the integrated system of ozonation followed by anaerobic degradation.
Technoscience Publications
Title: Integrated Method of Ozonation and Anaerobic Process for Treatment of Atrazine bearing Wastewater
Description:
The paper presents the treatment of atrazine-contaminated wastewater by ozonation followed by an anaerobic process using Upflow Anaerobic Sludge Blanket (UASB) reactor.
The experiment was performed with 100 ppb synthetic solutions of atrazine prepared in ultra-pure water.
The corresponding initial Chemical Oxygen Demand (COD) is 226 mg.
L-1.
The initial pH was adjusted to 9.
5.
The atrazine-bearing synthetic wastewater was ozonated with an ozone dose of 9.
4mg/l for 40 minutes of optimum ozonation time, resulting in a 35% reduction in the initial concentration of atrazine.
Along with atrazine reduction, there was a COD removal of 54.
42%.
Further, it was degraded with an anaerobic process, resulting in the final reduction in atrazine concentration of 81% and the corresponding removal in COD of 86.
7%.
The process of ozonation led to the mineralization of atrazine and enhancement in the biodegradability of the wastewater.
Using ion chromatography, the ozonated wastewater sample was analyzed for ionic by-products before and after ozonation.
The ion chromatography results showed the breaking of the atrazine compound and the formation of Cl-, NO3-, SO42-, and F- as intermediate products.
Further, the BOD5/COD ratio increased, reflecting the increased biodegradability.
This ozonated wastewater was treated in a UASB reactor where the pesticide was degraded to 19 ppb, and COs degraded to 30 mg.
L-1.
The overall removal of atrazine pesticide and COD were 81% and 86.
7%, respectively, in the integrated system of ozonation followed by anaerobic degradation.
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