Denitrification and dissimilatory nitrate reduction to ammonium in digested sludge

1981 ◽  
Vol 27 (9) ◽  
pp. 878-885 ◽  
Author(s):  
Heinrich F. Kaspar ◽  
James M. Tiedje ◽  
Richard B. Firestone

Acetylene inhibition and 13N methods were used to assay digested sludge for its potential to denitrify and to reduce nitrate to ammonium. At nitrate concentrations below 10 μM, the reduction of N2O to N2 was not inhibited by acetylene concentrations as high as 80 kPa, though at higher nitrate concentrations acetylene was an effective inhibitor. NO, N2O, and N2 were produces immediately after addition of nitrate or nitrite, indicating that denitrifying enzymes were present. NO was maintained at a concentration of 2–5 nM, while nitrate or nitrite were being reduced, but this gas was depleted once the ionic N oxide substrates were exhausted. Acetylene had little effect on appearance and disappearance of NO. It was also noted that NO was readily consumed by chemical reactions in the anaerobic sludge. Added N2O was reduced without a lag, but pasteurized samples did not consume N2O although they produced it. Fresh digested sludge reduced 60–70% of the added 13NO3− to 13NH4+ with the rest of the NO3−-N presumably lost to denitrification. This agrees well with the nitrate partitioning observed by the acetylene inhibition method in which 30–40% of the NO3−-N was recovered as N2O. Denitrification capacity persisted in both digested sludge and methanogenic enrichment culture which had been grown in a chemostat for 2.5 years with acetate and ammonium as the solid carbon and nitrogen source. This suggests that denitrifiers with capacities for alternative anaerobic energy metabolism may be more common than now known.

2006 ◽  
Vol 1 (3) ◽  
Author(s):  
Bernd Heinzmann ◽  
Gerd Engel

In 1994 for the first time massive incrustations in the centrifuges treating the digested sludge were detected in some wastewater treatment plants (WWTP’s) of the Berliner Wasserbetriebe, which were, as was found out later, mainly due to the precipitation of white MAP (magnesium ammonium phosphate = struvite) deposits with small portions of different calcium phosphate compounds. The reason for this was the over saturation of the digested sludge and the process water (from the separated centrate of the digested sludge) with carbon dioxide, the spontaneous release of or degassing of carbon dioxide, causing the pH to increase, thus altering the solubility equilibrium, and facilitating crystallisation, resulting in deposits (incrustations) on the walls. Obviously, the wastewater purification process used, with enhanced biological phosphorus removal and concentrated streams of digesting sludge, favours the formation of incrustations during sludge treatment. These incrustations were the cause of a lot of operational problems. To prevent incrustations, modifications in the process engineering technology have been applied after several studies and trials. Deliberate extraction of the CO2, e.g. by air injection through a fine-bubble surface aeration system at the bottom of the digested sludge storage tank just before the centrifuges, causes the pH to rise to approx. 8 and thus to cause induced struvite precipitation. This technology enables a precipitation product suitable for recycling to be generated and separated from the anaerobic sludge using a hydro-cyclone. A subsequent second hydro-cyclone stage allowed a further increase in the P-concentration to approx. 40 kg/m3, giving a yield of phosphorus of 20 %. This corresponds with P-load of approx. 316 kg/day and amounts to 18 % of the P inlet load in the WWTP Waßmannsdorf. It was shown that this experimental process is in principle suitable for the separation of the MAP precipitation product in the anaerobic sludge. A complete washing process for the raw MAP is not yet installed, and furthermore, to find the best sizes of nozzles in the hydro-cyclones and most effective pressures tests will have to be carried out soon at pilot level. A comparison with the minimum nutrients content for different kinds of fertiliser (super-phosphate, dicalcium-phosphate with magnesium, NP-fertiliser) defined by the German Fertiliser Regulations, shows that the precipitated MAP is within the range of other legally certified fertilisers. The MAP showed contaminant levels 5 times or more below the limit values of the German Sewage Sludge Ordinance. The MAP precipitation product is very soluble in different solvents (from ammonium chloride to hydrochloric acid). This implies that the precipitation product can be used as a long term fertilizer. In two test soils having a pH value of 6.6 and 7.1, the MAP precipitation solid was tested using standard ryegrass and showed good phosphorus availability from this material leading to a good grass growth.


1973 ◽  
Vol 8 (1) ◽  
pp. 26-35
Author(s):  
K.S. Hogg ◽  
J. Ganczarczyk

Abstract The aerobic sludge digestion system at the sewage treatment plant at Dunnville, Ontario was designed as a one-stage aeration process (by means of the Inka system) of moderately concentrated excess activated sludge (less than 1 percent of TS), followed by continuous sludge thickening and sludge drying lagoons for the final dewatering of the digestion product. An evaluation of this system was conducted in the summer of 1972. It included the study of sludge and supernatant characteristics, phosphorus balance and an economical comparison of the costs associated with this type of aerobic digestion and anaerobic sludge digestion for similar size (about 1.7 IMGD) activated sludge process plants. Results of the investigations disclosed that the aerobic digester with sludge loading of about 0.03 lb VS/cu ft/day and an average hydraulic detention time of only 9.2 days, operated satisfactorily at the summer climatic conditions of Southern Ontario. This process, however, could not be judged on the basis of volatile solids reduction, which proved to be only equal to 6 percent. This phenomenon was probably due to the solubility in water of a part of the mineral constituents of the sludge under the process conditions. The change in the sludge specific oxygen uptake rates from 8.9 to 2.75 mg 02/gVSS/hr at 25°C, was a more reliable indicator of the digested sludge characteristics. Supernatant quality (average COD of 170 mg/l and SS of 110 mg/l) and the dewaterability of the digested sludge (average resistance to filtration equal to 0.86 x 1013 m/kg) provided additional information of the digester’s performance.


2008 ◽  
Vol 57 (2) ◽  
pp. 231-236 ◽  
Author(s):  
J. Huang ◽  
M. Elektorowicz ◽  
J. A. Oleszkiewicz

The objectives of the study were to upgrade sewage sludge to Class A Exceptional Quality biosolids (as defined by US EPA) using an electrokinetics dewatering system. The pathogens monitored were Salmonella spp, and fecal coliforms (FC). Ten bench-scale electrokinetic cells were set up for the disinfection of the following sludges: primary, secondary (attached growth culture and suspended culture), and anaerobically digested sludge. A conditioning liquid was also added to five cells. Blower system to aid in dewatering and drying was used in in four EK cells. Sludge characteristics such as water content, volatile solids content, sulfate and chloride ions concentrations, FC and Salmonella spp. before and after the tests were monitored. The highest total solids content (98% TS) was achieved in the cell with the low voltage gradient, in the presence of the conditioner and with the blower system. An average reduction by 50% of volatile solids was observed. The highest, 11 log-reduction of Salmonella spp. was observed in a cell with anaerobically digested sludge. No fecal coliforms were observed in any of the cells after EK treatment.


1994 ◽  
Vol 40 (8) ◽  
pp. 645-650 ◽  
Author(s):  
María M. Dobao ◽  
Manuel Martínez-Luque ◽  
Conrado Moreno-Vivián ◽  
Francisco Castillo

The phototrophic bacterium Rhodobacter capsulatus E1F1 possesses an assimilatory, inducible nitrate reductase that is regulated by carbon and nitrogen metabolism. Nitrate reductase activity was detected in cells cultured with amino acids and nitrate as simultaneous nitrogen source but it required an additional carbon source such as D,L-malate. A significant rise in nitrate reductase activity was observed in media with increasing nitrate concentrations up to 10 mM KNO3, although higher nitrate concentrations had an inhibitory effect. Growth yield, generation time, and nitrate reductase activity were also dependent on the concentration of D,L-malate in cells growing with 10 mM nitrate. In carbon-starved cells, nitrate reductase activity dropped even in the presence of nitrate. The intracellular concentration of keto acids such as oxaloacetate or 2-oxoglutarate fluctuated widely depending on the presence of nitrogen and carbon sources in the culture medium. The increase in the intracellular concentration of oxaloacetate or 2-oxoglutarate in R. capsulatus E1F1 correlated well with a rise in nitrate reductase activity. These results suggest that the intracellular carbon–nitrogen balance regulates nitrate uptake in R. capsulatus E1F1, thus affecting the expression of nitrate reductase.Key words: carbon–nitrogen balance, nitrate reductase, Rhodobacter capsulatus.


2010 ◽  
Vol 62 (2) ◽  
pp. 427-434 ◽  
Author(s):  
P. Jenicek ◽  
J. Koubova ◽  
J. Bindzar ◽  
J. Zabranska

The paper reviews results and experience of microaerobic experiments at both high and low sulphide concentrations and evaluates advantages and drawbacks of the anaerobic digestion of sludge in microaerobic conditions as regards biogas quality, digested sludge quality, organic pollutants biodegradability and methanogenic activity of biomass. The innovative microaerobic modification of the anaerobic sludge digestion technology was studied in both laboratory and full scale. Microaerobic conditions are obtained by dosing of a limited amount of the air into the liquid phase of the anaerobic digester. It was shown that anaerobic bacteria including methanogens can be active also in such system. In a mixed culture, even strict anaerobes can survive without inhibition, if the facultative microorganisms are able to consume the present oxygen quickly and fully. Until now, the microaerobic conditions were predominantly used for hydrogen sulphide removal from biogas. In the paper the role of the surplus oxygen was studied also at low sulphide concentration, when the oxygen is consumed in high extent for other processes beside sulphide oxidation.


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