Treatment of organic synthesis wastewater using anaerobic packed bed and aerobic suspended growth bioreactors

The performance of an anaerobic mesophilic packed bed reactor, with a mixture of GAC and tezontle, followed by an aerobic suspended growth system was studied for the treatment of organic chemical wastewater with a high COD concentration (22-29 g/L). The testing of the anaerobic-aerobic system was co...

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Veröffentlicht in:Water science and technology : a journal of the International Association on Water Pollution Research. - 1986. - 55(2007), 7 vom: 11., Seite 235-43
1. Verfasser: Mijaylova-Nacheva, P (VerfasserIn)
Weitere Verfasser: Ramírez-Camperos, E, Cuevas-Velasco, S
Format: Aufsatz
Sprache:English
Veröffentlicht: 2007
Zugriff auf das übergeordnete Werk:Water science and technology : a journal of the International Association on Water Pollution Research
Schlagworte:Journal Article Organic Chemicals Water Pollutants, Chemical Nitrogen N762921K75 Oxygen S88TT14065
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245 1 0 |a Treatment of organic synthesis wastewater using anaerobic packed bed and aerobic suspended growth bioreactors 
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520 |a The performance of an anaerobic mesophilic packed bed reactor, with a mixture of GAC and tezontle, followed by an aerobic suspended growth system was studied for the treatment of organic chemical wastewater with a high COD concentration (22-29 g/L). The testing of the anaerobic-aerobic system was conducted in an experimental set-up for almost 2.5 years. Different operational conditions were evaluated. The anaerobic reactor showed performance stability and COD removals higher than 80% were obtained with loads up to 16.6 kg x m(-3) x d(-1). The acclimation of the aerobic biomass to the substrate in the anaerobic effluent was very quick and COD removals higher than 94% were obtained even at high organic loads. The combined anaerobic-aerobic system allowed total COD removals higher than 99.5% and the accomplishment of the discharge requirements of 200 mgCOD/L when the anaerobic reactor was operated with loads of 8-11 kg x m(-3)x d(-1) and the aerobic reactor with 0.33 kg x kg(-1) x d(-1), being the total HRT of 4.4. The average TKN removal in the anaerobic-aerobic system was 97%, the average for the anaerobic reactor being 52% and that one for the aerobic system being 94% 
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700 1 |a Ramírez-Camperos, E  |e verfasserin  |4 aut 
700 1 |a Cuevas-Velasco, S  |e verfasserin  |4 aut 
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