Partial nitrification in a SHARON reactor in the presence of salts and organic carbon compounds

Short- and long-term effects of temperature on the Anammox process

The application of the Anammox process has been usually focused on the treatment of wastewater with temperatures around 30 degrees C in order to operate under optimum conditions. In this work, the feasibility of the application of the Anammox process at lower temperatures has been tested. First, the short-term effects of temperature on the Anammox biomass were studied using batch tests. An activation energy of 63 kJ mol(-1) was calculated and the maximum activity was found at 35-40 degrees C. Activity tests done at 45 degrees C showed an irreversible loss of the activity due to the biomass lysis. A SBR was operated at different temperatures (from 30 to 15 degrees C) to determine the long-term effects. The system was successfully operated at 18 degrees C but when temperature was decreased to 15 degrees C, nitrite started to accumulate and the system lost its stability. Adaptation of biomass to low temperatures was observed when the specific activities obtained during first batch tests are compared to those obtained during the operation of the SBR.

Bacterial community dynamics and conversion of inorganic nitrogen under aerobic and micro-aerobic conditions

To investigate the inorganic nitrogen conversion in reactors that were operated under aerobic and micro-aerobic conditions and to identify populations that became acclimated in the reactors under those oxygen conditions, we operated two reactors with 72 h of hydraulic retention time and an artificial medium containing ammonium- and nitrite-nitrogen without any organic compound. We determined the concentration of inorganic nitrogen in samples from the reactors and the microbial community structure in the reactors by using PCR-DGGE of the partial 16S rRNA gene. The results showed that nitrification to nitrate fully progressed in the aerobic reactor within 24 h, but we could not find any obvious reaction in the micro-aerobic reactor. In a view of microbial community structure, the total number of microorganisms composing the communities in the reactors was dramatically decreased compared to those of the initial inoculated sludge that originated from the Jang-lim sewage treatment plant in Busan, Republic of Korea because of the limited nutrients present. One Nitrospira sp. was clearly detected under both aerobic (as DO > 2 mg l(-1)) and micro-aerobic (as DO < 0.7 mg l(-1)) conditions while no AOB-like bacterium was exactly matched among main bands. By the results, nitrite-oxidizing bacteria may be more tolerant to variations in oxygen, or the occupation of ammonia-oxidizing bacteria as dominant groups may have been inhibited by substrate starvation and high concentrations of nitrite-N in influent.

Ammonium removal from solution using ion exchange on to MesoLite, an equilibrium study

This paper investigates the potential of MesoLite ion exchange media for ammonium (NH(4)(+)) removal from solution in the presence of competing cations. Batch tests were performed under a range of conditions to assess the effect of contact time, solution pH and solution concentration on the performance and capacity of the media for this application. The data obtained was fitted to the Langmuir and Freundlich isotherm models with the Langmuir model providing the better description of the process. Results indicate a maximum equilibrium capacity of 49g NH(4)(+)Nkg(-1) of media is achievable under the experimental conditions studied. A detailed examination of the data shows that increasing solution concentration and increased contact time provide the best performance at an optimum pH of between 6 and 7.

Novel partial nitritation treatment for anaerobic digestion liquor of swine wastewater using swim-bed technology

A swim-bed reactor using the biofringe acryl-fiber biomass carrier was used for partial nitritation treatment for anaerobic digestion liquor of swine wastewater. The sludge in the reactor demonstrated excellent settling properties, and the sludge volumetric index (SVI) was always about 50 ml g(-1). The mixed liquor suspended solids (MLSS) concentration was maintained above 10,000 mg l(-1) with a maximum of 16,800 mg l(-1). Satisfactory and stable partial nitritation was obtained at a nitrogen loading rate (NLR) of 1.9 kg-N m(-3) d(-1) without any operational control. Only a little nitrate was produced almost during the whole operational period and the nitrite to total oxidized nitrogen ratio (NO(2)-N/(NO(2)-N+NO(3)-N)) was always above 95%. In addition, the influence of temperature on partial nitritation efficiencies was also investigated and non-controlled efficiencies were maintained stably between 15 degrees C and 30 degrees C at an NLR of 1.9 kg-N m(-3) d(-1), but suddenly deteriorated when the temperature fell below 15 degrees C. Nitrite oxidizing bacteria were inhibited by free ammonia and free nitric acid, which prevented the conversion of nitrite to nitrate and the inhibition due to free nitric acid weaken with a decrease in temperature. It was apparent that these phenomena were crucial to the control of partial nitritation treatment.