298 94 307/02 Untersuchungen zum Stand der Umsetzung des ...
298 94 307/02 Untersuchungen zum Stand der Umsetzung des ... 298 94 307/02 Untersuchungen zum Stand der Umsetzung des ...
Example plants Teil 3 Seite 8-34 Corporate clarification plant of the Kraftisried animal carcass disposal plant, 87647 Unterthingau Corporate clarification plant of the East Bavarian Meat Flour Association,94447 Plattling Corporate clarification plant of the Eiweiß- und Fettverwertung GmbH & Co, 49191 Belm-Icker, Germany Clarification plant of the Union for Animal Carcass Disposal (Zweckverband für Tierkör- perbeseitigung) Lenz, 01561 Lenz, Germany Rethmann TBA Genthin GmbH, 39307 Mützel, Germany Oberding animal carcass disposal plant, Germany 8.2.4.1.2 Description 8.2.5 Neutralisation tanks (AT3535005) Neutralisation stages are necessary, for example, when high pH values result from strip- ping or extremely low pH values result from ammonia conversion. Since high salanisation takes place as a result, it needs to be tested precisely whether a neutralisation process is required. At the Oberding animal carcass disposal plant, for example, the neutralisation process with 31 per cent hydrochloric acid leads to an increase in spec. conductibility of 17 to 33% (at a pH value of the effluent of approx. 10 in terms of inflow and 7,5 in terms of outflow). Achieved environmental benefits Cross media effects Operational data Applicability Economics Driving force for implementation Example plants Oberding animal carcass disposal plant, Germany Corporate clarification plant of the Kraftisried animal carcass disposal plant, 87647 Unterthingau Reference literature ATV-Handbuch Industrieabwasser (Dienstleistungs und Veredelungsindustrie) Biological methods Aerobic part-treatment The aerobic part-treatment can refer to the reduction of the organic carbon compounds, but also to a partly nitrification. In regard to the reduction of organic carbon compounds,
Teil 3 Seite 8-35 one often tries to achieve a purification degree at which the cleaned wastewater resem- bles municipal raw wastewater. Anaerobic preliminary wastewater treatment Because of the composition of the wastewater from the meat meal industry, this waste- water should be very suitable for anaerobic pre-treatment. However, the elimination of the nitrogen can not be achieved in anaerobic method. Furthermore, it is always possible to achieve only part-elimination of the organic pollutant load, so that this can be used only for preliminary wastewater treatment. An anaerobic pre-treatment of the wastewater is eligible especially in case of indirect discharged combined with a physical-chemical nitrogen elimination. In order to achieve high volume-time exploitation degrees simultaneous with a high process stability, the ap- plication of fixed bed reactors with wastewater recirculation has proved to be the most efficient of the modern anaerobic technologies with biomass retention. Table 8-4 shows the degradation rates of an installed anaerobic preliminary treatment. Table 8-4: Influent and effluent data of an anaerobic pre-treatment plant Parameter Influent Effluent February July In~/decreas e % Influent Effluent In~/decreas e pH 7,5 7,8 + 4 7,9 8,2 3,8 spec. conductivity mS/c m 6,67 6,89 + 3,2 7,54 7,66 + 1,6 Filterable solids mg/l 1.115 532 - 61,8 2.642 1.011 - 62 COD total mg/l 4.311 1.156 - 73,2 9.414 2.208 - 76,5 BOD5 total mg/l 3.433 534 - 84,5 5.890 1.154 - 80,4 Fat mg/l 370 90,8 - 75,5 717 265 - 63 NH4-N mg/l 126 145 + 15,1 185 208 + 12,4 org.-N mg/l 57,6 30,4 - 47,2 80,2 59,4 - 25,9 P total mg/l 8,7 8,6 - 0,7 14,5 12,8 - 12,1 Sulphide mg/l 24,1 8 - 66,8 8,1 13,5 + 65,2 Sulphate mg/l 39,5 11 - 72,2 65,5 22,8 - 65,2 Central biological wastewater treatment Generally, for the central wastewater treatment with nitrogen elimination, the following wastewater treatment methods are used for TBAs: - single-stage activation methods with preliminary denitrification for additional wastewa- ter treatment measures (such as pressure biology with large internal recirculation flow for biomass concentration through membrane filtration), - single-stage activation methods with simultaneous denitrification in undivided activa- tion tanks, - single-stage activation methods with alternating or intermittent denitrification, %
- Seite 305 und 306: Teil 3 Seite 6-18 ceous earth filte
- Seite 307 und 308: See description under 1 Limed bone
- Seite 309 und 310: H Concentration See description und
- Seite 311 und 312: Teil 3 Seite 6-24 The excess acid i
- Seite 313 und 314: Teil 3 Seite 7-1 7 CURRENT CONSUMPT
- Seite 315 und 316: 7.1.1 Rendering 7.1.1.1 Water Teil
- Seite 317 und 318: Teil 3 Seite 7-5 - Cleaning wastewa
- Seite 319 und 320: Teil 3 Seite 7-7 Table 7-5 shows th
- Seite 321 und 322: 7.1.2 Fat melting 7.1.3 Fish meal a
- Seite 323 und 324: Teil 3 Seite 8-1 8 TECHNIQUES TO CO
- Seite 325 und 326: Reference literature Teil 3 Seite 8
- Seite 327 und 328: Teil 3 Seite 8-5 Corporate clarific
- Seite 329 und 330: Economics Driving force for impleme
- Seite 331 und 332: 8.1.9 Rubishes Teil 3 Seite 8-9 8.1
- Seite 333 und 334: Oberding animal carcass disposal pl
- Seite 335 und 336: Operational data Applicability Econ
- Seite 337 und 338: Teil 3 Seite 8-15 Corporate clarifi
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- Seite 341 und 342: Continuous sterilisation Teil 3 Sei
- Seite 343 und 344: Teil 3 Seite 8-21 through a system
- Seite 345 und 346: Cross media effects Operational dat
- Seite 347 und 348: Teil 3 Seite 8-25 The energy requir
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- Seite 351 und 352: Teil 3 Seite 8-29 Corporate clarifi
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- Seite 355: Teil 3 Seite 8-33 Table 8-3: Perfor
- Seite 359 und 360: Teil 3 Seite 8-37 storage rooms and
- Seite 361 und 362: Teil 3 Seite 8-39 Rethmann TBA Gent
- Seite 363 und 364: Teil 3 Seite 9-1 9 BEST AVAILABLE T
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- Seite 367 und 368: Investition Re-Invest © 150 TDM 50
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Teil 3 Seite 8-35<br />
one often tries to achieve a purification degree at which the cleaned wastewater resem-<br />
bles municipal raw wastewater.<br />
Anaerobic preliminary wastewater treatment<br />
Because of the composition of the wastewater from the meat meal industry, this waste-<br />
water should be very suitable for anaerobic pre-treatment. However, the elimination of the<br />
nitrogen can not be achieved in anaerobic method. Furthermore, it is always possible to<br />
achieve only part-elimination of the organic pollutant load, so that this can be used only for<br />
preliminary wastewater treatment.<br />
An anaerobic pre-treatment of the wastewater is eligible especially in case of indirect<br />
discharged combined with a physical-chemical nitrogen elimination. In or<strong>der</strong> to achieve<br />
high volume-time exploitation degrees simultaneous with a high process stability, the ap-<br />
plication of fixed bed reactors with wastewater recirculation has proved to be the most<br />
efficient of the mo<strong>der</strong>n anaerobic technologies with biomass retention.<br />
Table 8-4 shows the degradation rates of an installed anaerobic preliminary treatment.<br />
Table 8-4: Influent and effluent data of an anaerobic pre-treatment plant<br />
Parameter Influent Effluent<br />
February July<br />
In~/decreas<br />
e<br />
%<br />
Influent<br />
Effluent In~/decreas<br />
e<br />
pH 7,5 7,8 + 4 7,9 8,2 3,8<br />
spec. conductivity<br />
mS/c<br />
m<br />
6,67 6,89 + 3,2 7,54 7,66 + 1,6<br />
Filterable solids mg/l 1.115 532 - 61,8 2.642 1.011 - 62<br />
COD total mg/l 4.311 1.156 - 73,2 9.414 2.208 - 76,5<br />
BOD5 total mg/l 3.433 534 - 84,5 5.890 1.154 - 80,4<br />
Fat mg/l 370 90,8 - 75,5 717 265 - 63<br />
NH4-N mg/l 126 145 + 15,1 185 208 + 12,4<br />
org.-N mg/l 57,6 30,4 - 47,2 80,2 59,4 - 25,9<br />
P total mg/l 8,7 8,6 - 0,7 14,5 12,8 - 12,1<br />
Sulphide mg/l 24,1 8 - 66,8 8,1 13,5 + 65,2<br />
Sulphate mg/l 39,5 11 - 72,2 65,5 22,8 - 65,2<br />
Central biological wastewater treatment<br />
Generally, for the central wastewater treatment with nitrogen elimination, the following<br />
wastewater treatment methods are used for TBAs:<br />
- single-stage activation methods with preliminary denitrification for additional wastewa-<br />
ter treatment measures (such as pressure biology with large internal recirculation flow<br />
for biomass concentration through membrane filtration),<br />
- single-stage activation methods with simultaneous denitrification in undivided activa-<br />
tion tanks,<br />
- single-stage activation methods with alternating or intermittent denitrification,<br />
%