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tion, contain the lowest possible concentrations of volatile free fatty acids which are<br />

evaporated in particular as a result of high temperatures (� 130 °C) during drying.<br />

Achieved environmental benefits<br />

The ammonia from the water vapour from ren<strong>der</strong>ing is converted into an easy to use fer-<br />

tilizer, where 25% of the nitrogen comes from the ren<strong>der</strong>ing process. This fertilizer can<br />

replace the same product where all the nitrogen is chemically synthesized from molecular<br />

nitrogen from air with about 1 kg of fuel oil consumption per kg of synthesized nitrogen.<br />

On the other hand, nitrogen removal from waste water from ren<strong>der</strong>ing can be avoided<br />

where ammonia is converted back into molecular nitrogen by bacterial processes (nitrifica-<br />

tion and denitrification).<br />

Cross media effects<br />

The only immediate product of the process is a concentrated ammonium nitrate solution<br />

(typically 55%) and an acidic vapour containing low molecular carboxylic acids (acetic<br />

acid, propionic acid, butyric acid and others). These acids are ideal substrates for aerobic<br />

and anaerobic waste water treatment processes, where they contribute either to the pro-<br />

duction of biomasss or to the production of biogas. The nitric acid used to convert ammo-<br />

nia into the corresponding ammonium cation can be a waste acid from nitrification proc-<br />

esses in concentrations below 50%.<br />

Operational data Applicability<br />

The process can be used everywhere, where the water from drying during the ren<strong>der</strong>ing<br />

process is still in the vapour form. This vapour can then flow through the packed column<br />

before it is used in a second evaporating stage or condensed without any secondary use.<br />

Economics<br />

This process avoids the energy consuming biological nitrification and denitrification for<br />

the removal of nitrogen from condensed water vapour from ren<strong>der</strong>ing processes. The<br />

main energy consuming device in this process is the pump for the slightly acidic ammo-<br />

nium nitrate solution.<br />

Driving force for implementation<br />

Easy control of ammonia nitrogen in water vapour from ren<strong>der</strong>ing. The nitrogen content<br />

in the acidic vapour leaving the process can even be adapted to the nitrogen demand in<br />

the subsequent biological waste water treatment plant.<br />

The product formed in this process can easily be sold as a fertilizer in all countries,<br />

where a concentrated ammonium nitrate urea solution containing 28% N is used as liquid<br />

fertilizer.<br />

Example plants<br />

Currently, this type of ammonia converter is utilised at the Brögbern (Lingen) and Regau<br />

(Upper Austria) animal carcass disposal plants (comp. 4.12.1c). The converter at the

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