Treatment of olive mill wastewaters by ozonation, aerobic degradation and the combination of both treatments
Identifieur interne : 000714 ( Main/Exploration ); précédent : 000713; suivant : 000715Treatment of olive mill wastewaters by ozonation, aerobic degradation and the combination of both treatments
Auteurs : F Javier Benitez [Espagne] ; Jesus Beltran Eredia [Espagne] ; Joaquin Torregrosa [Espagne] ; Juan L. Acero [Espagne]Source :
- Journal of Chemical Technology & Biotechnology [ 0268-2575 ] ; 1999-07.
English descriptors
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Abstract
The degradation of the pollutant organic matter present in olive oil mill wastewaters (OMW) is carried out by a single ozonation, a single aerobic degradation, and the combination of two successives steps: an ozonation followed by an aerobic degradation, and an aerobic degradation followed by an ozonation. In both single processes, the removal of this contaminant load is followed by means of global parameters which are directly related to the concentration of organic compounds in those effluents: chemical oxygen demand and total aromatic and phenolic contents. In the ozonation, an approximate kinetic study is performed which leads to the evaluation of the apparent kinetic constants for the aromatic reduction, kA. In the aerobic degradation, the kinetic study is conducted by using the Grau model, which is applied to the experimental data, and leads to the determination of the kinetic parameters of this model, K2 and n. In the combined processes, a higher COD global reduction is obtained by the successive stages, and an improvement in the removal of the organic material during the second treatment of both processes due to the pretreatment conducted is also observed. This enhancement is shown by an increase of the kinetic parameters (K2 and n in the aerobic degradation of the pre‐ozonated wastewaters; the apparent constant kA in the ozonation of the wastewaters preliminary fermented aerobically), in relation to the values obtained for them in the single processes carried out at the same operating conditions. © 1999 Society of Chemical Industry
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DOI: 10.1002/(SICI)1097-4660(199907)74:7<639::AID-JCTB92>3.0.CO;2-I
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In both single processes, the removal of this contaminant load is followed by means of global parameters which are directly related to the concentration of organic compounds in those effluents: chemical oxygen demand and total aromatic and phenolic contents. In the ozonation, an approximate kinetic study is performed which leads to the evaluation of the apparent kinetic constants for the aromatic reduction, kA. In the aerobic degradation, the kinetic study is conducted by using the Grau model, which is applied to the experimental data, and leads to the determination of the kinetic parameters of this model, K2 and n. In the combined processes, a higher COD global reduction is obtained by the successive stages, and an improvement in the removal of the organic material during the second treatment of both processes due to the pretreatment conducted is also observed. This enhancement is shown by an increase of the kinetic parameters (K2 and n in the aerobic degradation of the pre‐ozonated wastewaters; the apparent constant kA in the ozonation of the wastewaters preliminary fermented aerobically), in relation to the values obtained for them in the single processes carried out at the same operating conditions. © 1999 Society of Chemical Industry</div></front></TEI><affiliations><list><country><li>Espagne</li></country><region><li>Estrémadure</li></region><orgName><li>Université d'Estrémadure</li></orgName></list><tree><country name="Espagne"><region name="Estrémadure"><name sortKey="Benitez, F Javier" sort="Benitez, F Javier" uniqKey="Benitez F" first="F Javier" last="Benitez">F Javier Benitez</name></region><name sortKey="Acero, Juan L" sort="Acero, Juan L" uniqKey="Acero J" first="Juan L" last="Acero">Juan L. Acero</name><name sortKey="Beltran Eredia, Jesus" sort="Beltran Eredia, Jesus" uniqKey="Beltran Eredia J" first="Jesus" last="Beltran Eredia">Jesus Beltran Eredia</name><name sortKey="Torregrosa, Joaquin" sort="Torregrosa, Joaquin" uniqKey="Torregrosa J" first="Joaquin" last="Torregrosa">Joaquin Torregrosa</name></country></tree></affiliations></record>Pour manipuler ce document sous Unix (Dilib)
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