(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 ...
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
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
- 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 and 134: 122 Picture 30.: The heat exchanger
- Page 135: 124 used for the construction of l<
- 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
- Page 185 and 186: 174 (26,650) of all households acro
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