(best examples and good practices) on household organic waste ...

(best examples and good practices) on household organic waste ... (best examples and good practices) on household organic waste ...

11.11.2014 Views

125 technology is the reduction of the waste air flow to be treated to the technically feasible minimum with simultaneous concentration of the TOC content contained in the waste air. In the thermal-regenerative waste air cleaning process, the process air loaded with hydrocarbons is first heated using a ceramic heat exchanger module ong>andong> then fed to the heating chambers situated above it, in which complete oxidation of the hydrocarbons to form carbon dioxide ong>andong> water is ensured by a defined temperature level (>850 °C) ong>andong> a defined retention time (>2 sec.). (Wastesum project Del 3A., 2010) During the subsequent passing of the second ceramic heat exchanger, 98% of the heat energy taken up is returned to the heat exchanger. By cyclically switching over the 3 heat exchangers present, associated with intermediate flushing cycles for the prevention of “switching peaks”, continuous operation that conforms with the requirements is guaranteed, even for the varying input concentrations that typically occur in the treatment of residual waste. (Figure 36.) shows the schematic flow of the Dresden plant in Germany. Figure 36.: Process diagram of the Dresden plant in Germany. (Wastesum projectDel 3A., 2010) 7.3.5.TW Eldena grass drier In Germany operates a grass drier facility in Eldena. The facility has been supplied with a VADEB DDD grass dryer, model DX-2000 by ‘ Vong>andong>enbroek

126 International’. In the Drum Drying system the product is directly heated. The exhaust gas flows directly into the rotating drum. Picture 32.: Grass drier facility The maximum drum inlet temperature is 650 o Celsius. The total volume of the dryer exhaust is treated by de-dusting equipment ong>andong> if needed, scrubber/condenser equipment. By recycling a part of the dryer (Figure 37.) exhaust gas to the dryer, the amount of airborne gas to the stack is strongly reduced. Figure 37.: The DDD drying system The facility has an Evaporation capacity of16.000 l/h, a grass input capacity of 20.000 kg/h at 20% DS ong>andong> a grass output capacity of 4.500 kg/h at 90% DS. Finally the facility has a need for thermal energy consumption of: 3,4 Mjoule/kg

126<br />

Internati<strong>on</strong>al’. In the Drum Drying system the product is directly heated. The<br />

exhaust gas flows directly into the rotating drum.<br />

Picture 32.: Grass drier facility<br />

The maximum drum inlet temperature is 650 o Celsius. The total volume of the<br />

dryer exhaust is treated by de-dusting equipment <str<strong>on</strong>g>and</str<strong>on</strong>g> if needed,<br />

scrubber/c<strong>on</strong>denser equipment. By recycling a part of the dryer (Figure 37.)<br />

exhaust gas to the dryer, the amount of airborne gas to the stack is str<strong>on</strong>gly<br />

reduced.<br />

Figure 37.: The DDD drying system<br />

The facility has an Evaporati<strong>on</strong> capacity of16.000 l/h, a grass input capacity of<br />

20.000 kg/h at 20% DS <str<strong>on</strong>g>and</str<strong>on</strong>g> a grass output capacity of 4.500 kg/h at 90% DS.<br />

Finally the facility has a need for thermal energy c<strong>on</strong>sumpti<strong>on</strong> of: 3,4 Mjoule/kg

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