(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 ...
123 separation between light (combustible)
124 used for the construction of l
- Page 83 and 84: 72 within solution under the influe
- Page 85 and 86: 74 material, and t
- Page 87 and 88: 76 changing pole configuration or w
- Page 89 and 90: 78 4.7. Mechanical Biological Treat
- Page 91 and 92: 80 Biological processing compartmen
- Page 93 and 94: 82 equivalence considerations <stro
- Page 95 and 96: 84 5.2. Waste streams considered in
- Page 97 and 98: 86 Figure 27.: Percentage of munici
- Page 99 and 100: 88 6.Italy The Italian strategy Ita
- Page 101 and 102: 90 Italy also set targets for colle
- Page 103 and 104: 92 (Figure 30.). The quality of com
- Page 105 and 106: 94 a controlled environment with wa
- Page 107 and 108: 96 Picture 11.: The Corteolona plan
- Page 109 and 110: 98 The building in the foreground h
- Page 111 and 112: 100 compost their garden waste. The
- Page 113 and 114: 102 The total amount of waste produ
- Page 115 and 116: 104 7. Germany 7.1. Waste managemen
- Page 117 and 118: 106 has been specified only for som
- Page 119 and 120: 108 7.3. Best practices</st
- Page 121 and 122: 110 The installation has different
- Page 123 and 124: 112 The sludge is placed into a lar
- Page 125 and 126: 114 Picture 22.: Air mixing mechani
- Page 127 and 128: 116 Finally the dried sludge is bee
- Page 129 and 130: 118 process treats the wastes as co
- Page 131 and 132: 120 consumption is about 0.7 x106 k
- Page 133: 122 Picture 30.: The heat exchanger
- Page 137 and 138: 126 International’. In the Drum D
- Page 139 and 140: 128 Picture 34.: Delivery crane in
- Page 141 and 142: 130 industrial processes, where <st
- Page 143 and 144: 132 industry, mixes the waste <stro
- Page 145 and 146: 134 8. Sweden The Swedish strategy
- Page 147 and 148: 136 joint committee or local govern
- Page 149 and 150: 138 upon the number of collected fr
- Page 151 and 152: 140 2004 2005 2006 2007 2008 Hazard
- Page 153 and 154: 142 Anaerobic digestion also produc
- Page 155 and 156: 144 Hässleholm 12,300 10,120 Karls
- Page 157 and 158: 146 distributed either through gas
- Page 159 and 160: 148 mentioned in earlier. (Chemical
- Page 161 and 162: 150 Picture 39.: Public fuelling st
- Page 163 and 164: 152 The pumpable organic waste is b
- Page 165 and 166: 154 purchased by AGA and</s
- Page 167 and 168: 156 Picture 43.: Paper bag with hou
- Page 169 and 170: 158 (Table 8.): The Ljungsjöverket
- Page 171 and 172: 160 Figure 46.: Schematic operation
- Page 173 and 174: 162 9. United Kingdom The British S
- Page 175 and 176: 164 9.2. Waste quantities 2008 The
- Page 177 and 178: 166 9.3. Best practices</st
- Page 179 and 180: 168 The partners collect around 840
- Page 181 and 182: 170 Figure 51.: Quantity of waste c
- Page 183 and 184: 172 The company recycles wood, meta
123<br />
separati<strong>on</strong> between light (combustible) <str<strong>on</strong>g>and</str<strong>on</strong>g> heavy <strong>waste</strong> comp<strong>on</strong>ents (metals,<br />
inert materials) is achieved <str<strong>on</strong>g>and</str<strong>on</strong>g> thus a high fuel quality is guaranteed.<br />
The remaining ferrous <str<strong>on</strong>g>and</str<strong>on</strong>g> n<strong>on</strong>-ferrous c<strong>on</strong>stituents are removed from the dry,<br />
light weight material using magnetic <str<strong>on</strong>g>and</str<strong>on</strong>g> fluidized bed separators. This treated<br />
lightweight fracti<strong>on</strong> now c<strong>on</strong>sists of virtually 100% combustible materials such<br />
as wood, paper, plastics, textiles <str<strong>on</strong>g>and</str<strong>on</strong>g> <strong>organic</strong> matter. The average compositi<strong>on</strong><br />
of this SRF fracti<strong>on</strong> is shown in (Figure 35.). The renewable energy fracti<strong>on</strong><br />
c<strong>on</strong>tained in the stabilate is around 2/3 <str<strong>on</strong>g>and</str<strong>on</strong>g> could be beneficial for renewable<br />
energy generati<strong>on</strong>. (Wastesum projectDel 3A., 2010)<br />
The calorific value of the SRF lies within the range of 15–18 MJ/kg <str<strong>on</strong>g>and</str<strong>on</strong>g> thus<br />
represents the energy equivalent of treated, dried lignite coal. Due to its dry<br />
c<strong>on</strong>sistency, SRF is very easy to store <str<strong>on</strong>g>and</str<strong>on</strong>g> can thus be used as a sec<strong>on</strong>dary fuel<br />
in industrial processes when it is required <str<strong>on</strong>g>and</str<strong>on</strong>g> independent of the amount of<br />
<strong>waste</strong> generated. The removal of heavy metals associated with the removal of<br />
metal parts <str<strong>on</strong>g>and</str<strong>on</strong>g> batteries is of decisive importance for the use of SRF as a<br />
sec<strong>on</strong>dary fuel. It reduces the heavy metal load by up to 90% compared to that<br />
of residual <strong>waste</strong>.<br />
Figure 35.: Average compositi<strong>on</strong> of SRF of Dresden plant in Germany<br />
(Wastesum project Del 3A., 2010)<br />
The heavy fracti<strong>on</strong> gained from the initial density sorting process is subjected<br />
to further treatment stages. With the separati<strong>on</strong> of the combustible residues<br />
(<strong>organic</strong> matter, plastics), the overall <strong>organic</strong> c<strong>on</strong>tent (expressed as igniti<strong>on</strong><br />
losses) are reduced <str<strong>on</strong>g>and</str<strong>on</strong>g> a material quality is achieved that can for example be