2002
DOI: 10.1016/s0168-1656(02)00183-9
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Use of limestone for pH control in autotrophic denitrification: continuous flow experiments in pilot-scale packed bed reactors

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Cited by 65 publications
(21 citation statements)
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“…The pH during the experiment decreased from 6.8 to 6. A decrease in pH during carbohydrate fermentation has been also observed in other studies where powdered (Taylor & Nasr-El-Din, 2003) or coarse (Koenig & Liu, 2002;Maree et al, 2004;Maree & Duplessis, 1994) CaCO 3 was used as the neutralizing agent. After the substrate (glucose) was consumed (18 h), the remaining CO 2 was sparged out of the broth resulting in a rapid increase of the pH.…”
Section: Numerical Integrationsupporting
confidence: 72%
“…The pH during the experiment decreased from 6.8 to 6. A decrease in pH during carbohydrate fermentation has been also observed in other studies where powdered (Taylor & Nasr-El-Din, 2003) or coarse (Koenig & Liu, 2002;Maree et al, 2004;Maree & Duplessis, 1994) CaCO 3 was used as the neutralizing agent. After the substrate (glucose) was consumed (18 h), the remaining CO 2 was sparged out of the broth resulting in a rapid increase of the pH.…”
Section: Numerical Integrationsupporting
confidence: 72%
“…The specific rate of autotrophic denitrification was inhibited when pH decreased below 6.8 [55]. Zinc and copper ions inhibited the reaction, and yet the presence of trichloroethylene did not inhibit the reaction at the concentrations up to 20 mg/L [61].…”
Section: Inhibition and Mitigationmentioning
confidence: 93%
“…According to reaction stoichiometry as shown in Equation (3) [48], the sulphur-utilizing autotrophic denitrification process consumed about 4 g alkalinity (as CaCO 3 ) per g NO 3 -N reduced resulting in a decrease of pH [55], and to compensate that, limestone can be added to the system to increase pH. Based on established chemical-biological interactive relationships, an empirical formula was presented to determine the optimum sulphur to limestone ratio for nitrate removal, taking into account the characteristics of the influent wastewater [55]. The ratio of influent alkalinity to theoretically required alkalinity in the wastewater suggested a value of no less than 0.5 in order to prevent pH inhibition in nitrate removal performance [55].…”
Section: Effect Of Alkalinity and Supplementationmentioning
confidence: 99%
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“…The optimum pH for the growth of T. denitrificans is in the range of 6.8-8.2 [6]. In order to control pH, limestone is widely used as an alkalinity source in the SOD process with elemental sulfur as an electron donor [2,[7][8][9][10]. The combination of sulfur and calcium carbonate in the form of pellets as a single matrix also represented an alternative media for ensuring adequate alkalinity for the growth of sulfur oxidizing denitrifiers and for the reduction of clogging problem as well [11].…”
Section: Introductionmentioning
confidence: 99%