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 ...
Teil 3 Seite 4-25 sewage from slaughterhouse plants with sifting installations with a mesh size of 1 mm in terms of BSB5 represent a reduction of between 17 and 49%. However, if all above men- tioned internal measures are taken, and assuming efficient running of the plant in other respects, these values will be significantly lower. It is advisable to determine degrees of efficiency beforehand on the basis of semi-commercial trials. Screenings emanating from the red line should be ceded to an animal carcass disposal plant. The screenings emanating from the green line can possibly be utilised or composted ag- riculturally after they have been disinfected. Achieved environmental benefits Cross media effects Operational data Applicability Economics Driving force for implementation Example plants Corporate clarification plant of the Duringer Fleischkontor (During meat branch office), Germany Anaerobic waste treatment of the NFZ pork slaughterhouse in Emstek, District of Clop- penburg, Germany Pre-treatment slaughterhouse, North-Rhine Westphalia, waste water pre-treatment plant slaughterhouse, Saxony Anhalt, Germany Oberding animal carcass disposal plant, Germany Corporate clarification plant of the Kraftisried animal carcass disposal plant, 87647 Unterthingau Reference literature ATV-Handbuch Industrieabwasser (Lebensmittelindustrie) 4.5.2 Chemical/physical treatment Reference to actual BREF - Use of H2O2 to remove H2S from waste water in feather rendering plants (4.3.1.4- p.253)
Teil 3 Seite 4-26 4.5.2.1 Ammoniacal-N removal from rendering condensate by ammonia conversion Description An alternative method of reducing ammonia nitrogen in the water vapour from rendering processes is ammonia conversion. In contrast to stripping, the gaseous ammonia con- tained in vapours is already removed during this process. The ammonia, along with the vapours in this process is channelled into a washing column (converter) with a counter- flow stream of a slightly acidic nitrous acid solution, where the ammonia is converted into ammonium with nitrate as counter ion. The converter consists of a packed column, through which the slightly acidic ammonium nitrate solution is pumped into circulation (Figure 4-5). The ammonium nitrate is removed from the sump of the packed column upon reaching the desired concentration of 50 to 60%. The vapours freed from the ammonia are subsequently, as usual, condensed into now acidic vapour condensates in a con- denser. Currently, only vapours emanating from drying are channelled through the plant. A future conversion plant for cooker vapours is also planned. Acid Exhaust vapours Ammonium nitrate Ammonia con- verter Condenser Anaerobic reactor Aerobic after treatment Liquid phase Gas phase Figure 4-5: Diagram of ammonia conversion at the Brögbern animal carcass disposal plant Through the addition of a specific quantity of urea, a urea ammonium nitrate solution of 28% (UAN-28) can be produced from the ammonium nitrate solution obtained in this way, which can be utilised as a nitrogen rich agricultural fertiliser. It is also feasible to accom- modate the ammonium nitrate in industrial clarification plants for the purpose of nutrient amelioration. It is important during the operation of a converter of this type that the vapours do not contain any entrained solid matter. Appropriate cyclones and other suitable separation devices must therefore be installed preceding the converter. The vapours should, in addi-
- Seite 201 und 202: Schleswig-Holstein Niedersachsen No
- Seite 203 und 204: Teil 3 Seite 1-10 ceutical or techn
- Seite 205 und 206: Teil 3 Seite 1-12 Table 1-8: Compan
- Seite 207 und 208: Teil 3 Seite 1-14 The amount of ste
- Seite 209 und 210: Teil 3 Seite 2-1 2 PROCESSES AND TE
- Seite 211 und 212: 2.1.1.1 Lairage Teil 3 Seite 2-3 As
- Seite 213 und 214: Teil 3 Seite 2-5 the rumen is spin-
- Seite 215 und 216: 2.1.2.1 Delivery of birds 2.1.2.2 S
- Seite 217 und 218: Teil 3 Seite 2-9 Figure 2-3: Presen
- Seite 219 und 220: - Rinsing of the carcasses and carc
- Seite 221 und 222: Teil 3 Seite 3-4 the currently usua
- Seite 223 und 224: Zerlegung 2% Schlachtung 30% Schlac
- Seite 225 und 226: 3.1.3.4 Plucking 3.1.3.5 Eviscerati
- Seite 227 und 228: Liquid phase from the dewatering (y
- Seite 229 und 230: Teil 3 Seite 4-2 - Re- use of salt
- Seite 231 und 232: [to be completed] Main achieved env
- Seite 233 und 234: Teil 3 Seite 4-6 - Efficient use an
- Seite 235 und 236: Teil 3 Seite 4-8 heat exchangers, p
- Seite 237 und 238: Teil 3 Seite 4-10 The situation wit
- Seite 239 und 240: Teil 3 Seite 4-12 rect evaporation
- Seite 241 und 242: Teil 3 Seite 4-14 Additional heat e
- Seite 243 und 244: Weight loss after 24 hours Temperat
- Seite 245 und 246: 4.2.5 Evisceration Reference to act
- Seite 247 und 248: Achieved environmental benefits Cro
- Seite 249 und 250: 4.5.1 Mechanical treatment 4.5.1.1
- Seite 251: Teil 3 Seite 4-24 Both in terms of
- Seite 255 und 256: Teil 3 Seite 4-28 Brögbern animal
- Seite 257 und 258: Teil 3 Seite 4-30 The decision depe
- Seite 259 und 260: Teil 3 Seite 4-32 closed area can b
- Seite 261 und 262: Teil 3 Seite 4-34 coincides with th
- Seite 263 und 264: Teil 3 Seite 4-36 At a slaughterhou
- Seite 265 und 266: Age of sludge (tTS) Is this of spec
- Seite 267 und 268: Example plants Teil 3 Seite 4-40 Co
- Seite 269 und 270: BSB5 - load Bd (BSB ) NH4 -N - load
- Seite 271 und 272: Fe Fl Fe Fl P D MB Teil 3 Seite 4-4
- Seite 273 und 274: Teil 3 Seite 4-46 Parameters Unit M
- Seite 275 und 276: Teil 3 Seite 4-48 To optimise the m
- Seite 277 und 278: Driving force for implementation Ex
- Seite 279 und 280: Teil 3 Seite 4-52 Table 4-15 Dimens
- Seite 281 und 282: Teil 3 Seite 4-54 liquid fertiliser
- Seite 283 und 284: - No cross media effects Teil 3 Sei
- Seite 285 und 286: Teil 3 Seite 4-58 3. Filtermaterial
- Seite 287 und 288: Decomposition level Measure- Teil 3
- Seite 289 und 290: Teil 3 Seite 6-2 FAT/ HEAT TRANSFER
- Seite 291 und 292: Teil 3 Seite 6-4 Clarification plan
- Seite 293 und 294: Teil 3 Seite 6-6 ENERGY FAT/ HEAT C
- Seite 295 und 296: Teil 3 Seite 6-8 ENERGY/ STEAM INPU
- Seite 297 und 298: Teil 3 Seite 6-10 water if necessar
- Seite 299 und 300: Teil 3 Seite 6-12 - In- vessel comp
- Seite 301 und 302: Teil 3 Seite 6-14 For 1000 kg of de
Teil 3 Seite 4-25<br />
sewage from slaughterhouse plants with sifting installations with a mesh size of 1 mm in<br />
terms of BSB5 represent a reduction of between 17 and 49%. However, if all above men-<br />
tioned internal measures are taken, and assuming efficient running of the plant in other<br />
respects, these values will be significantly lower. It is advisable to determine degrees of<br />
efficiency beforehand on the basis of semi-commercial trials.<br />
Screenings emanating from the red line should be ceded to an animal carcass disposal<br />
plant.<br />
The screenings emanating from the green line can possibly be utilised or composted ag-<br />
riculturally after they have been disinfected.<br />
Achieved environmental benefits<br />
Cross media effects<br />
Operational data Applicability<br />
Economics<br />
Driving force for implementation<br />
Example plants<br />
Corporate clarification plant of the Duringer Fleischkontor (During meat branch office),<br />
Germany<br />
Anaerobic waste treatment of the NFZ pork slaughterhouse in Emstek, District of Clop-<br />
penburg, Germany<br />
Pre-treatment slaughterhouse, North-Rhine Westphalia, waste water pre-treatment plant<br />
slaughterhouse, Saxony Anhalt, Germany<br />
Oberding animal carcass disposal plant, Germany<br />
Corporate clarification plant of the Kraftisried animal carcass disposal plant, 87647<br />
Unterthingau<br />
Reference literature<br />
ATV-Handbuch Industrieabwasser (Lebensmittelindustrie)<br />
4.5.2 Chemical/physical treatment<br />
Reference to actual BREF<br />
- Use of H2O2 to remove H2S from waste water in feather ren<strong>der</strong>ing plants<br />
(4.3.1.4- p.253)