ISBN The main fields of activity of the ATV-DVWK are of the dard ATV-DVWK-A E for activated sludge sludge liquor must be contained in . STANDARDATV-DVWK-A EDimensioning of This ATV Standard has been elaborated by the ATV-DVWK Specialist Committees KA 5 and. Title: Activated Sludge Expert – Software for Standard ATV-DVWK-A E ” Dimensioning of Single-Stage Activated Sludge Plants” – Edition /
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DWA Shop – Software Activated Sludge Expert
Further information, in particular for concentrated wastewater from foodstuff production, is to be found in  and in the ATV Report “Bulking sludge, floating sludge and foam in activated sludge plants causes and combating”  [available in English].
The daily average remaining alkalinity is to be determined for the most unfavourable loading case, i. The denitrification tank is downstream from the nitrification tank; for safety reasons a post-aeration tank follows. However, an obligation for application can atvv from legal or administrative regulations, a contract or other legal reason.
The concentration of suspended solids depends essentially on functional capability of the secondary settling tanks with fluctuating hydraulic feeding, sludge volume index and the sludge removal as well as the return sludge ratio and waste sludge removal. With its application no one avoids responsibility for his own action or for the correct application in spe- In this Standard technical regulations are drawn up cific cases; this applies in particular for the correct ahv the dimensioning both for handling of the margins described in the Standard.
Channels and pump sumps for the collection of the activated sludge are useful for the emptying of tanks. With regard to the method of function one differentiates between horizontal and vertical flow secondary settling tanks. For vertical flow secondary settling tanks the effective surface area at the mid-point dvdk inlet aperture and water level is to be set, see Fig.
The settling behaviour of the activated sludge, characterised by the sludge volume index SVIin combination with the mixed liquor suspended solids concentration SSATinfluences the size of the secondary settling tanks and biological reactors.
Vorschau Atv Dvwk a 131e
Therefore a return loading may not be added, for example, globally as a percentage to all loads from the wastewater. In order to prevent the entry of floating sludge into the outlet pipes, the water level must be at least 20 cm above the inlet openings. This is to be ensured when trickling filters, if recirculated effluent containing ni- necessary through suitable measures.
With wastewater having a high fraction of readily biodegradable organic matter, the inclusion of an upstream selector is helpful; upstream anaerobic mixing tanks for excess biological phosphorus removal do also have such a selector effect, see Fig.
The bridge velocity vSR is the same as that for scraper bridges. Both denitrification tanks and nitrification tanks can be formed as cascades. It is defined as the quotient of the mass of suspended dry solids in the biological reactor VAT SSAT and the daily mass of dry solids of waste activated sludge.
With pure carbon removal and nitrification of the organic nitrogen introduced into the sludge without denitrification the retention time with dry digester is released as ammonium nitrogen.
An active aeration using energy is, as a rule, not required. The cascade type approximately with the biologically active surface.
ATV-DVWK-A E – Free Download PDF
Precipitation using iron Precipitation using aluminium 2. The dimensioning values presented below have been determined for disc biological contactors.
With this the following correlation can be made: With this the geometry of normal tank shapes is taken into account. Biological reactors, which are to be considered as completely mixed tanks, usually lead to higher sludge volume indices and tend rather to the development of filamentous bacterial atb than tanks with a concentration gradient, which are such which, for example, are formed as a cascade or in which a plug flow exists.
If the relevant loads have to be estimated using the connected inhabitants, the values in Table 1 can be used. The politically and economically independent association works nationally tav internationally in the fields of pollution control, wastewater, water-hazardous sub- stances, waste, hydraulic engineering, hydraulic power, hydrology, soil protection and contaminated sites.
This can also lead to a decrease in the pH value. The thickening achieved therein is dependent on the sludge properties SVIthe depth of the sludge layer, the thickening time and the type of the sludge removal system. For the transition area values can be taken from Table The biologically active surface is, as a rule, high loadings, so that it is advisable to limit the smaller than the theoretical surface of the sfiller BOD5 surface loading rate of the first stage with material.
With this Standard, planners and examiners receive a differentiated working basis for dimensioning single-stage activated sludge plants. Determination from the curve of the 2-week mean over two to three years. The discs nor- ensured. The loading capacity of an activated sludge plant is determined substantially by concentration of suspended solids SSAT of the activated sludge and the volume of aeration tank. Inlet The inlet design for vertical flow rectangular and circular tanks with flat bottoms equals that of horizontal flow secondary settling tanks.
In this respect some specifications previously introduced at as estimates or assumptions can be replaced by appropriately clear statements and the designation of influencing parameters – and in many cases, also confirmed. If the dimensioning capacity is determined based on the number of connected inhabitants, the inhabitant-specific BOD5 load for raw wastewater from Table dvwj is to be used.