کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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56618 | 47089 | 2010 | 7 صفحه PDF | دانلود رایگان |

This work is proposing a design strategy for an industrial combined solar photo-Fenton/aerobic biological system for the decontamination of wastewater polluted with commercial pesticides. The two possibilities (photo-Fenton/bio and Bio/photo-Fenton) of the combined system were evaluated (using different analytical tools and bioassays, mainly DOC, COD, toxicity and biodegradability) in pilot plant and the most successful was scaled-up. Photo-Fenton (20 mg/L of Fe2+) was carried out in compound parabolic collectors (CPC) at an initial DOC of 500 mg/L (100 mg/L of each commercial pesticide). The biological pilot reactor was an Immobilized Biomass Reactor (IBR) filled with polypropylene Pall Ring® supports colonized by activated sludge. The industrial plant has a total collector surface of 150 m2, total photo reactor volume of 1060 L and the scaled-up biological treatment plant (also an IBR) consists basically of two IBRs (1230 L each).The photo-Fenton treatment at pilot plant scale was able to reduce toxicity (from 96% to 50% of inhibition) and increase biodegradability (from 50% to 95%) of the wastewater and the most suitable point for combining it with the biological treatment was after the total elimination of the active ingredients. The efficiency of the combined photo-Fenton/bio system in terms of mineralization was 94%, of which 35.5% corresponds to the AOP and 58.5% to the aerobic biological treatment. The combination Bio/photo-Fenton was not successful. The efficiency of the industrial-scale combined system (photo-Fenton/bio) was 84%, 35% corresponding to the photo-Fenton treatment and 49% to the biological stage.
Journal: Catalysis Today - Volume 151, Issues 1–2, 15 April 2010, Pages 100–106