Biomedical subjects

S Tarre

Publications and source records attributed to S Tarre.

5 recordsLinked to original sources

PubMed2002

Nitrification utilizing CaCO3 as the buffering agent.

Nitrification utilizing chalk (calcium carbonate) as the buffering agent was investigated. Three different fluidized bed reactor configurations were examined in order to study the effect of reactor layout on nitrification and concomitant chalk dissolution. The first system consisted of two interconnected columns with high recycle rate, one containing zeolite as the carrier for the nitrifying biomass and the other chalk as the buffering agent. The second reactor system consisted of a single column containing both zeolite and chalk particles. In the third system, nitrification was carried out in a single column where chalk particles were used both as the carrier for the biomass and as the buffer. Results showed that only the reactor with chalk acting as both the buffering agent and the biomass carrier could be operated without external buffer (NaHCO3) addition. This system operated at high ammonium removal rates of up to 2.5 g N l(-1) reactor d(-1) even though the bulk solution of the reactor had a low pH of 5.5. The high nitrification efficiency at this low pH was probably mainly a result of a favorable microenvironment surrounding the nitrifying biomass attached to the chalk.

Antacids↗

PubMed2002

Production of gaseous nitrogen compounds in a novel process for ammonium removal.

The production of gaseous nitrogen compounds, particularly the greenhouse gas nitrous oxide, was investigated in a novel process for ammonium removal from wastewater. The process is based on the adsorption of ammonium on zeolite followed by bioregeneration. The zeolite serves the dual purpose of an ion exchanger and a physical carrier for nitrifying bacteria which bio-regenerate the ammonium saturated mineral. An analysis of the nitrifying population composition in the reactor fed with simulated secondary effluent (NH4+ = 50 mg/l) revealed that about half of the bacteria in the biofilm were common ammonium oxidizers Nitrosococcus mobilis and Nitrosomonas, while the other half were nitrite oxidizers. The amount of nitrogen losses, under different conditions, and the identification of the emitted gases (N2 or N2O) were investigated in two sets of experiments: (I) batch experiments using biomass originating from the ion exchange reactor with and without the addition of nitrite, and (II) continuous experiments using the ion exchange reactor with zeolite as the biomass carrier. In the batch experiments, nitrite and oxygen concentrations were determined as the major parameters responsible for the formation of gaseous nitrogen gas during ammonia oxidation by autotrophic bacteria. Continuous experiments showed that the major parameter significantly affecting nitrogen losses was the amount of ammonium adsorbed by the zeolite during the ion exchange phase. The amount of ammonium adsorbed determines the ammonium concentration during the initial period of bioregeneration, which in turn directly influences oxygen demand and the resulting concentrations of oxygen and nitrite. It was concluded that the formation of nitrogen gas compounds in the ion exchange/bioregeneration process can be eliminated by adjusting the operational regime to have a shorter adsorption phase resulting in smaller amounts of ammonium adsorbed per cycle.

Adsorption↗

PubMed2001

Chalk as the carrier for nitrifying biofilm in a fluidized bed reactor.

A fluidized bed reactor for nitrification with chalk as the biomass carrier and the sole buffer agent was studied. Chalk dissolution in the reactor was found to follow the stoichiometric ratio of 1 mole of CaCO3 dissolved for each mole of NH4+ oxidized. Three batches of chalk, each one having a different dissolution rate, were used to replace the dissolved chalk. The three dissolution rates resulted in three different steady state pH levels in the reactor (4.7-6.6) and nitrification rates. Nitrification was found to be limited by either the chalk dissolution rate or dissolved oxygen concentration depending on the type of chalk used. A maximal nitrification rate of 1.44 g NH4(+)-N/l reactor.d was observed. The average cell yield was 0.1 g cells/g N oxidized, similar to the cell yield during reactor start-up when the pH was 7. The specific ammonium oxidation rates varied between 0.08 and 0.15 mg NH4(+)-N oxidized/mg protein.h, values which are in the reported range for nitrification at pH 7 to 8. Oxygen update rate (OUR) results indicated that the major mechanism responsible for the high nitrification rate observed in the reactor operating at low pH seems to be the favorable microenvironment provided by the chalk.

Bacteria↗

PubMed2001

Ammonium removal using a novel unsaturated flow biological filter with passive aeration.

A novel vertical bed process for the removal of ammonium from secondary effluents, using a "passive air pump", has been developed. The process is based on convective aeration caused by a fill and draw operational sequence, and combines the advantages of the vertical wetlands concept with the high loading rates typically associated with trickling filters. Experiments were carried out in a 500-l reactor using simulative effluents and actual municipal secondary effluents. A maximal ammonium removal rate of 1100 g N/m2 reactor/d was achieved using simulative effluents and an effective gravel size of 0.96 mm. At all hydraulic loads applied, the nitrification rate was found to be limited by the oxygen transfer rate. The small-size medium used with simulative effluents clogged when using actual municipal secondary effluents. Two other media (2.46 mm and 4.31 mm) did not clog during the entire experimental period and a maximum removal load of 300 g N/m2 reactor/d was achieved. This value is still much higher than typical rates reported for conventional vertical beds.

Filtration↗

PubMed1994

Precipitation potential as a major factor in the formation of granular sludge in an upflow sludge-blanket reactor for denitrification of drinking water.

The effects of the chemical composition of water on granular sludge formation and characteristics in a denitrifying upflow sludge-blanket (USB) reactor were studied. Denitrification of drinking water showed different biomass sludge characteristics when the reactor was fed with groundwater as opposed to surface water USB reactors fed with groundwater produced granules with good settling characteristics, SVI (sludge volume index) values lower than 30 ml/g, and high reactor biomass concentrations (20-25 g/l), while surface-water-fed reactors exhibited lower biomass concentrations (10-15 g/l) due to poor settling characteristics (SVI values of 50-90 ml/g). Sludge granules from the reactor fed with surface water had a low mineral content of between 10% and 20% as compared to a mineral content of 25%-50% in the groundwater reactor. The larger mineral content in the groundwater-fed reactor was due to a greater precipitation potential, i.e. higher concentrations of calcium and alkalinity present in groundwater combined with the release of alkalinity and subsequent increase in pH caused by biological denitrification. Verification for this phenomenon was established by enriching surface water with calcium and alkalinity, which increased the reactor's precipitation potential from 15 mg/l to 40 mg/l (as CaCO3). The granules obtained from the reactor fed with enriched surface water had a high mineral content of between 40% and 50% and very low SVI values, contributing to improved granule-settling characteristics and reactor stability.

Biomass↗