Construccion de lecho nitrificante. Construccion de lecho nitrificante. Image may contain: one or more people and outdoor. English (US); Español · Français. Determinación del diámetro óptimo de zeolita para el asentamiento de bacterias nitrificantes en un reactor de lecho fluidizado para eliminar nitrógeno. Lo que se busca es la eliminaciÛn de los nitratos que contaminan las aguas empleando bacterias nitrificantes. El soporte que se emplea para que las bacterias.
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Ecological Applications 22 3pp. COD T results are shown in Fig. L -1 on the sixteenth day and a slight increase until the end of the experiment. This decrease was followed by a slight increase following days.
May 12 th Firstly, with a total recirculation and later, when the recirculation rate was chosen, the feeding was started. This state corresponds with the maximum of the adhesion curves.
Once confirmed that no leakage or conduction problems occurred, 8 L of the synthetic industrial nitificantes liquid were introduced within the column.
Water Research 24 3pp. A first run was performed with water to verify the state of the seals and the general operation of each system component Fig. For the 1 nitrificantez diameter case, a minimum for the TSS value mg. June 13 th At the experiment end TSS values were constant. In this case, the preferred zeolite particle size for the fluidized bed reactor was between 0. Wiley and Sons, New York, For nitrificanets present study, the zeolite is crushed and classified granulometrically.
COD T results are shown in Fig.
Lechos nitrificantes | Spanish to English | Architecture
The constant levels of biomass must to be maintained. This result is in accordance with the adherence maximum nitrifocantes for the same day. Applied Geochemistry 27, pp. The final 20 cm corresponded to an inverted truncated cone with a 20 cm diameter base Fig. There activated carbon support was used, with a density ranging from 0.
Removal of nitrogen present in the wastewater resulting from domestic and industrial activities is usually carried out combining biological processes of nitrification and denitrification, since costs are lower compared to the physical and chemical processes. Each sampling day, the zeolite and liquid of both mini-digesters from one of the pair for the three different zeolite diameters were analyzed. It can be seen that there was an almost complete biodegradation of organic matter in all samples for the different diameters, being Activation and free ammonia inhibition.
Removal during drinking water treatment and human risk assessment. If we compare Tables 4 and 6we can lexhos that the pH is maintained constant during 21 days. June 4 th Environmental Toxicology and Chemistry 31 6pp.
Table 1 details the composition of the feeding liquid and Table 2 shows that of the saline solution used to prepare the synthetic industrial waste liquid. The extracted zeolite was placed on a filter paper on a capsule and introduced into a hot oven for six hours to ensure complete drying of the support. The acrylic column had two side outlets located at 25 and 70 cm from the top.
Therefore, concentration of dissolved oxygen in water must be kept around 2 to 3 mg. First modification related to the employed microbial support . In these systems, granular activated carbon, sand and clay are used as microbial support [1, ]. However, 1 mm is chosen to achieve higher adhesion values.
ComparablePropertiesIn , Comparable Properties
To nltrificantes a proper implementation of the fluidized bed aerobic reactor a number of biological, chemical and physical parameters such as temperature, pH, microbial support, volume, feeding rate, retention time, and the reactor dimensions and configuration must be taken into account .
TSS comprises both microorganisms and every substance that is suspended in the liquid industrial waste; however, VSS refers only to the microorganisms. I Microbes that reproduce by fission or nitridicantes budding. However, this is not an acidic enough pH to avoid the life of microorganisms, so this diameter zeolite may perform its metabolic functions, but not optimally. M and Heijnen, J.
Peer comments on this answer and responses from the answerer agree. L -1 was reached. Microbial adhesion For the microbial adhesion tests, assemble of 16 mini digesters were used with a volume of mL, for each one of the zeolite diameters Fig. After this initial time zeolite and liquid samples were taken every two or three days.
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A suitable approach to restore the environmental quality of the Odiel river basin. A similar behaviour was observed for the 2 mm zeolite diameter case, the TSS was initially roughly constant and then an abrupt decrease from mg.
The feeding pump was connected to a timer to achieve the necessary inflow. Biotechnology Bioeng 21, pp.