2003
DOI: 10.1016/s0043-1354(02)00119-7
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Congruence in the performance of model nitrifying activated sludge plants located in Germany, Scotland and Spain

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Cited by 11 publications
(7 citation statements)
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“…Activated sludge from Leixlip I WWTP was used to seed the reactors at start-up. The reactors were operated with a food-to-microorganism (f/m) ratio of 0.13 kg COD kg -1 day -1 using the synthetic wastewater described above, with sodium bicarbonate (NaHCO 3 ) added to final concentration of 0.3 g L -1 synthetic wastewater to prevent a drop in pH due to nitrification (Christofi et al 2003). Distilled, deionized water was used to prepare the synthetic wastewater and for dilution to the desired COD.…”
Section: Acclimatization Proceduresmentioning
confidence: 99%
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“…Activated sludge from Leixlip I WWTP was used to seed the reactors at start-up. The reactors were operated with a food-to-microorganism (f/m) ratio of 0.13 kg COD kg -1 day -1 using the synthetic wastewater described above, with sodium bicarbonate (NaHCO 3 ) added to final concentration of 0.3 g L -1 synthetic wastewater to prevent a drop in pH due to nitrification (Christofi et al 2003). Distilled, deionized water was used to prepare the synthetic wastewater and for dilution to the desired COD.…”
Section: Acclimatization Proceduresmentioning
confidence: 99%
“…Rather than demonstrating a higher tolerance to shock loads of metal contaminants, the activated sludge from the industrial WWTP (Leixlip II) was more inhibited by AMD than activated sludge from municipal WWTPs. It is likely that the population of microorganisms in the industrial sludge has adapted to the presence of a specific industrial effluent (Christofi et al 2003), and consequently has a decreased resilience to shock loads of other toxicants. Using activated sludge from WWTPs treating MWW can ensure that the population of microorganisms has not become adapted to a specific industrial wastewater and is therefore more robust to changes in metal concentrations or pH shocks caused by adding AMD.…”
Section: Acute Toxicity Testsmentioning
confidence: 99%
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“…During each cycle, 1.7 L effluent was decanted and replaced with synthetic sewage (i.e., 50% volumetric exchange ratio) giving a HRT of 1 day (Ndon, 2007). OECD synthetic sewage (Christofi et al, 2003;Gendig et al, 2003) was used as the feed for the lab-scale plant. The 100-fold concentrated stock solution was stored at -sewage reservoir and to provide the desired sludge loading of 0.1 g BOD 5 g…”
Section: Laboratory-scale Sequencing Batch Reactors (Sbrs)mentioning
confidence: 99%
“…To avoided a decrease in the reactor pH during nitrification, as slightly acidic conditions are known to adversely affect the ciliate community (Cybis and Horan, 1997), NaHCO 3 was added to the synthetic sewage at a final concentration of 0.6 g L -1 (Christofi et al, 2003). The storage containers were kept cooled at an approximate temperature of 4-10˚C 100 to reduce bacterial growth and prevent degradation of the sewage.…”
Section: Laboratory-scale Sequencing Batch Reactors (Sbrs)mentioning
confidence: 99%