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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Elsevier Science 38, pp.
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To build the fluidized bed reactor, the design proposed by Navarro and Palladino, was used with some modifications. Water Research 24 3pp. Later on the fourteenth day and for the three cases, a decreasing behaviour was observed until curves reached a nearly constant value at the experiment end. However for the 0.
Author wants to give thanks to University of Vigo for the financial support given. The nitrificanyes efficiencies correspond to low flow rates and high organic loads.
L -1 that was reached on the fourteenth day. View forum View forum without registering on UserVoice. In these systems, granular activated carbon, sand and clay are used as microbial support [1, ].
Different control parameters were nitrificantee at the beginning and end of the operation. This state corresponds with the maximum of the adhesion curves. One of the most important variables in reactor design is the density of the aerobic fluidized bed material, as it affects the bed hydrodynamics and nitrificantws a direct effect on power consumption . Abstract In this work, the determination of the diameter of zeolite as a support for a microbial aerobic fluidized bed reactor is performed.
Upon receipt of the zeolite from the supplier, the grinding was started to obtain the required diameters lechoe. This increase is associated to the cryptic growth stage of the microorganisms natural cycle growth curvewhich takes place after the death phase.
Both side outlets with a 2. A life cycle assessment perspective. That made it useful to be included in fluidized bed reactors. This was loaded onto the column to achieve a fixed bed height of 15 cm. Mini-digesters were grouped in pairs, for elchos zeolite diameter. L -1 eleventh day to mg.
Identification and qualification of microorganism in activated sludge and biofilms by FISH. Environmental International 32, pp. The initial region of the adhesion increase, shown in Fig.
Tuning of the reactor. However, this is not an acidic enough nigrificantes to avoid the life of microorganisms, so this diameter zeolite may perform its metabolic functions, but not optimally. Graphs and results for each performed analyses are presented below.
As shown in Table 5after crushing and sieving enough zeolite intrificantes each of the expected sizes 0. You can request verification for native languages by completing a simple application that takes only a couple of minutes. At the experiment end TSS values were constant. A first run was performed with water to verify the state of the seals and the general operation of each system component Fig. Later on the fourteenth day and for the three cases, a decreasing behaviour was observed until curves reached a nearly constant value at the experiment end.
ComparablePropertiesIn , Comparable Properties
A first run was performed with water to verify the state of the seals and the general operation of each system component Fig. To ensure 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 .
To build the fluidized bed reactor, the design proposed by Navarro and Palladino, was used with some modifications. There is not significant differences in the measured microbial adhesion for the three diameters 0.
Then there is a slight increase in the seventeenth day followed by a fall back to values similar to the one of the fourteenth day.
It must be noted that particles should not be fragile as because of their continuous movement they can collide and become fragmented, changing their fluidizing characteristics and thus making even more difficult the control of the nitrifficantes expansion.
Tuning of the aerobic fluidized bed reactor. You have native languages that can be verified You can request verification for native languages by completing a simple application that takes only a couple of minutes. Finally, in the case of the zeolite with 1 mm diameter, VSS values showed a continuous fluctuation along the whole experiment time, with a lechs of mg.
The reactor was in operation for 21 days like the mini-digesters.
Reviewing applications can be fun and only takes a few minutes. The final 20 cm corresponded to an inverted truncated cone with a 20 cm diameter base Fig. To determine the mass of the adhered solids the following expression can be applied: Nitrificajtes initial region of the adhesion increase, shown in Fig.