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Driving force for implementation Example plants Teil 3 Seite 4-31 At the Kraftisried animal carcass disposal plant, a flotation system is in use for as yet unhomogenised waste water (system by the company Mangold), in which air is injected through submersed aerators. The flotation objects are removed from the surface by means of a paddle stirring device. An automatic spraying system prevents the possibly substantial formation of foam during flotation. Given a dimension for Q of a maximum of 15 m 3 /h, it exhibits a volume of 12 m 3 and a surface area of 8 m 2 . Concerning fat content, an elimination rate of 76% is achieved, and the COD (homogenised) is reduced by up to 42%. Table 4-4 illustrates the entire elimination capacity of the mechanical/physical- chemical stage, consisting of fat separators, cylindrical sieves and flotation. Table 4-4: Inflow and outflow values in terms of mechanical/physical-chemical effluent pre-treatment at the Kraftisried animal carcass disposal plant (mean value on the basis of daily composite samples; n = 3 to 111) Parameters Inflow Outflow In-/decrease % ces pH 9,0 - 9,5 7,7 - 11 - filterable substan- mg/l 1.530 570 - 62,7 COD total mg/l 5.024 3.416 - 32 Fat mg/l 1.590 199 - 87,5 NH4-N mg/l 943 648 - 31,3 org.-N mg/l 119 39 - 66,9 At the Oberding animal carcass disposal plant flotation takes place on the basis of a mix- ing and equalising basin. It is dimensioned for a constant effluent inflow of up to 8 m 3 /h. At this plant, a fat elimination rate of 50% was achieved. The COD (homogenised) is only reduced by 16%, since the excess sludge from the biological treatment plant simultane- ously reaches the flotation plant. This can lead to temporary overloading, so that even an increase in organic content material may result in comparison to in-flowing effluent. In terms of flotation plants, stripping of ammonia cannot be avoided due to a high con- tent of ammonia/ammonia concentrations in the effluent. At the Oberding animal carcass disposal plant the N-elimination carried out in this way amounted to 10%; at the Kraftisried animal carcass disposal plant, with higher initial values in the effluent, it amounted to approx. 30 to 40%. This means high ammonia contamination of the air in the enclosed flotation area, and therefore also the endangerment of personnel, since the permissible MAC values are exceeded by a wide margin. In addition, flotation plants are generally a source of strong odour emissions. In terms of enclosed accommodation of such a flotation plant, sufficient air extraction is therefore recommended. The air extracted from the en-

Teil 3 Seite 4-32 closed area can be utilised in compressors and in this way fed into the ventilators for the biological treatment plant. Oberding animal carcass treatment plant, Germany, Kraftesried animal carcass treat- ment plant, 87647 Unterthingau, Germany Corporate clarification plant of the East Bavarian Meat Flour Association,94447 Plattling Clarification plant of the Union for Animal Carcass Disposal (Zweckverband für Tierkör- perbeseitigung) Lenz, 01561 Lenz, Germany Rethmann TBA Genthin GmbH, 39307 Mützel, Germany Waste water pre-treatment for Bauerngut Fleisch- und Wurstwaren GmbH, Könnern, Germany, Anaerobic waste treatment of the NFZ pork slaughterhouse in Emstek, District of Cloppenburg, Germany Pre-treatment slaughterhouse, North-Rhine Westphalia, waste water pre-treatment plant slaughterhouse, Saxony Anhalt, Germany Reference literature ATV-Handbuch Industrieabwasser (Dienstleistungs und Veredelungsindustrie) ATV-Handbuch Industrieabwasser (Lebensmittelindustrie) 4.5.2.6 Chemical and physical techniques (AT3535005) Description Achieved environmental benefits Cross media effects Operational data Applicability Economics Driving force for implementation Example plants Oberding animal carcass disposal plant, Germany Reference literature 4.5.3 Biological treatment Normally, the existing production wastewater from slaughterhouses and meat production plants are discharged into municipal sewage systems and conveyed to central mechani- cal-biological wastewater treatment plants. As the organic substances contained in this wastewater are easily bio-degradable, it is not difficult to subject them to a full treatment together with domestic wastewater.

Driving force for implementation<br />

Example plants<br />

Teil 3 Seite 4-31<br />

At the Kraftisried animal carcass disposal plant, a flotation system is in use for as yet<br />

unhomogenised waste water (system by the company Mangold), in which air is injected<br />

through submersed aerators. The flotation objects are removed from the surface by<br />

means of a paddle stirring device. An automatic spraying system prevents the possibly<br />

substantial formation of foam during flotation. Given a dimension for Q of a maximum of<br />

15 m 3 /h, it exhibits a volume of 12 m 3 and a surface area of 8 m 2 . Concerning fat content,<br />

an elimination rate of 76% is achieved, and the COD (homogenised) is reduced by up to<br />

42%. Table 4-4 illustrates the entire elimination capacity of the mechanical/physical-<br />

chemical stage, consisting of fat separators, cylindrical sieves and flotation.<br />

Table 4-4: Inflow and outflow values in terms of mechanical/physical-chemical effluent<br />

pre-treatment at the Kraftisried animal carcass disposal plant (mean value on<br />

the basis of daily composite samples; n = 3 to 111)<br />

Parameters Inflow Outflow In-/decrease %<br />

ces<br />

pH 9,0 - 9,5 7,7 - 11 -<br />

filterable substan-<br />

mg/l 1.530 570 - 62,7<br />

COD total mg/l 5.<strong>02</strong>4 3.416 - 32<br />

Fat mg/l 1.590 199 - 87,5<br />

NH4-N mg/l <strong>94</strong>3 648 - 31,3<br />

org.-N mg/l 119 39 - 66,9<br />

At the Oberding animal carcass disposal plant flotation takes place on the basis of a mix-<br />

ing and equalising basin. It is dimensioned for a constant effluent inflow of up to 8 m 3 /h. At<br />

this plant, a fat elimination rate of 50% was achieved. The COD (homogenised) is only<br />

reduced by 16%, since the excess sludge from the biological treatment plant simultane-<br />

ously reaches the flotation plant. This can lead to temporary overloading, so that even an<br />

increase in organic content material may result in comparison to in-flowing effluent.<br />

In terms of flotation plants, stripping of ammonia cannot be avoided due to a high con-<br />

tent of ammonia/ammonia concentrations in the effluent. At the Oberding animal carcass<br />

disposal plant the N-elimination carried out in this way amounted to 10%; at the Kraftisried<br />

animal carcass disposal plant, with higher initial values in the effluent, it amounted to<br />

approx. 30 to 40%. This means high ammonia contamination of the air in the enclosed<br />

flotation area, and therefore also the endangerment of personnel, since the permissible<br />

MAC values are exceeded by a wide margin. In addition, flotation plants are generally a<br />

source of strong odour emissions. In terms of enclosed accommodation of such a flotation<br />

plant, sufficient air extraction is therefore recommended. The air extracted from the en-

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