2011
DOI: 10.1002/clen.201000199
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Effects of Fenton Pre‐Treatment on Waste Activated Sludge Properties

Abstract: Research Article Effects of Fenton Pre-Treatment on Waste Activated Sludge PropertiesFenton process was investigated for the purpose of biological sludge disintegration. The Box-Wilson experimental design was employed to evaluate the effects of major process variables (Fe(II) and H 2 O 2 concentrations) on both disintegration and dewatering performance of sludge. Results showed that 4 g Fe(II)/kg total solids (TSs) and 60 g H 2 O 2 /kg TS are efficient for floc disintegration. Fenton pre-treatment enhanced the… Show more

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Cited by 39 publications
(31 citation statements)
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“…Thus, Fenton pre-treatment enhanced methane production by 15% compared to the raw sludge digestion. These results are in line with those reported by Erden and Filibeli [10], where 19.4% higher methane production was obtained compared to raw sludge. The increase in the SCOD increases the methane production [10].…”
Section: Methane Production During Anaerobic Digestionsupporting
confidence: 95%
See 2 more Smart Citations
“…Thus, Fenton pre-treatment enhanced methane production by 15% compared to the raw sludge digestion. These results are in line with those reported by Erden and Filibeli [10], where 19.4% higher methane production was obtained compared to raw sludge. The increase in the SCOD increases the methane production [10].…”
Section: Methane Production During Anaerobic Digestionsupporting
confidence: 95%
“…These results are in line with those reported by Erden and Filibeli [10], where 19.4% higher methane production was obtained compared to raw sludge. The increase in the SCOD increases the methane production [10]. Erden and Filibeli [9] concluded that the specific methane production increased during the first 20 days of digestion in the digester containing Fenton pre-treated sludge.…”
Section: Methane Production During Anaerobic Digestionsupporting
confidence: 95%
See 1 more Smart Citation
“…into ferrous species (Fe 2? ) at the nZVI surface can occur when compared to the homogeneous oxidation [36]. Figure 2 illustrates the results obtained in terms of C-CO 2 released as a function of the mass of nZVI added, and it is possible to observe that the quantity of oxidized carbon is doubled when about 75 g of nZVI per kg TS -1 was added.…”
Section: Chemical Stabilisation Trialsmentioning
confidence: 90%
“…Globally, hydrogen peroxide catalysed by the iron catalyst leads to the production of hydroxyl radicals that are able to destroy the complex organic structures of the flocks. The soluble low molecular weight by-products may reach the liquid and be further oxidized in that phase [36]. The percentage of oxidized organic carbon was determined by two different methods based on TOC in the treated solid (Method 1) and in VS (Method 2).…”
Section: Chemical Stabilisation Trialsmentioning
confidence: 99%