The main aim of this research is to compare the efficiency of biological and chemical-physical treatments for the removal of organic azo dyes in the textile wastewater. Regarding the biological reduction of the wastewater colour the anaerobic/aerobic (ANA/AER) sequential step-treatment provides the best reductions in colour and COD. A lab-scale Sequencing Batch Reactor (SBR) fed with synthetic wastewater and mono-azo dye (at the initial concentration of 25 mg/l) was used achieving 84% colour reduction and 82% COD removal. Chemical-physical treatments were performed using the oxidative method with Fenton s reagent and adsorption on the activated carbon achieving respectively colour reduction over 90% (from the initial concentration of 250 mg/l) and 155 mg col/g GAC total adsorption capacity (from the initial concentration of 1 g/l).

Comparison between biological and chemical-physical treatment for colour removal / Farabegoli, Geneve; L., Pietrelli; Rolle, Enrico; A., Sabene. - ELETTRONICO. - (2004), pp. 65-72. (Intervento presentato al convegno 4th IWA World Water Congress and Exhibition tenutosi a Marrakech, Morocco nel 19-24 September) [10.2166/ws.2004.0094].

Comparison between biological and chemical-physical treatment for colour removal

FARABEGOLI, Geneve;ROLLE, Enrico;
2004

Abstract

The main aim of this research is to compare the efficiency of biological and chemical-physical treatments for the removal of organic azo dyes in the textile wastewater. Regarding the biological reduction of the wastewater colour the anaerobic/aerobic (ANA/AER) sequential step-treatment provides the best reductions in colour and COD. A lab-scale Sequencing Batch Reactor (SBR) fed with synthetic wastewater and mono-azo dye (at the initial concentration of 25 mg/l) was used achieving 84% colour reduction and 82% COD removal. Chemical-physical treatments were performed using the oxidative method with Fenton s reagent and adsorption on the activated carbon achieving respectively colour reduction over 90% (from the initial concentration of 250 mg/l) and 155 mg col/g GAC total adsorption capacity (from the initial concentration of 1 g/l).
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11573/324775
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