2011
DOI: 10.1016/j.cej.2011.05.098
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Comparison of several combined/integrated biological-AOPs setups for the treatment of municipal landfill leachate: Minimization of operating costs and effluent toxicity

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Cited by 113 publications
(37 citation statements)
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“…As reported in Section 3, the combination of aerated biological treatments and physical-chemical ones is the most used. Indeed, as is visible in Table 3, the results obtained allow considering these practices as reliable for COD and NH4-N removal, with special emphasis on AOP technologies with biological ones, also suggested in previous years and considered reliable solutions [177][178][179]. However, all of them do not achieve concentrations low enough to release the wastewater to water bodies and further treatments must to be applied such as membrane filtration.…”
Section: Discussionmentioning
confidence: 88%
“…As reported in Section 3, the combination of aerated biological treatments and physical-chemical ones is the most used. Indeed, as is visible in Table 3, the results obtained allow considering these practices as reliable for COD and NH4-N removal, with special emphasis on AOP technologies with biological ones, also suggested in previous years and considered reliable solutions [177][178][179]. However, all of them do not achieve concentrations low enough to release the wastewater to water bodies and further treatments must to be applied such as membrane filtration.…”
Section: Discussionmentioning
confidence: 88%
“…Furthermore, nutrient imbalances such as high ammonium nitrogen, low phosphorus and biologically degradable carbon content frequently occur in landfill leachate and make it difficult to maintain proper biological treatment and decent effluent quality. Therefore, post-treatment of biological effluents is still necessary to further remove organic matter [4,5]. The aforementioned limitations of biological techniques in addition to restrictive environmental legislations and the need for cost-effective treatments have led to an increased interest in the use of (advanced) oxidation processes ((A)OPs) such as Fenton, photocatalysis, UV/H 2 O 2 and ozonation as a valuable addition to conventional treatment techniques [6][7][8][9][10][11][12][13].…”
Section: Introductionmentioning
confidence: 99%
“…Jordá et al [14] reported a treatment cost of 0.74 €/m 3 for a paracetamol-containing wastewater ($1 mM; 100 mg DOC/L) using a photo-Fenton system. Cassano et al [15] reported the operating costs for the combination of a sequential batch biofilter granular reactor (SBBGR) and a solar photo-Fenton (SphF) process for the treatment of municipal landfill leachate (COD i = 2.8-3.6 g/L; DOC i = 0.9-1.2 g/L; N-NH 4,i = 1.5-2.0 g/L). The operating costs were 3.26 €/m 3 (2.54 €/m 3 for SBBGR and 0.72 €/m 3 for SphF) and 4.13 €/m 3 (2.54 €/m 3 for SBBGR and 1.59 €/m 3 for SphF) for a final COD of 500 and 160 mg O 2 /L, respectively.…”
Section: Introductionmentioning
confidence: 99%