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207 order to fully stabilize the end compost. 85% of the compost is cured in this facility b. Inside the warehouse where the compost is cured, the material is placed in windrows. The warehouse protects the compost from the outside environmental conditions. The windrows have a maximum height of 3.5 m. The residence time is 1 month. 15% of the compost is cured in this installation. Following the curing stage, the loaders feed the packaging unit, in order to package the end compost. (Morocomp.,2010) Packaging Unit The packaging unit consists of the following: a. Smoothening sub-unit for ameliorating the texture of the end product b. Sub-unit for placing the end compost inside bags <strong>and</strong> for sealing these bags c. Sub-unit of palletizing the packaged end compost Wastewater Treatment Unit The wastewater that is treated in this unit is generated from: a. The reception unit for the trucks b. The unit of mechanical separation c. The composting unit (leachate collected from the floor of the composting tunnel) d. Wastewater from all the sanitation areas of the factory A two-stage aerobic biological process takes place for the treatment of wastewater. The final effluent is used for irrigating the grass facilities of the installation Unit for Treatment of Air Emissions from the Mechanical Separation Unit This unit treats the air emissions resulting for the Unit of Mechanical Separation. The treatment unit consists of three (3) biofilters for treating air exhausts from the unit of mechanical separation. Each biofilter corresponds to one reservoir of the unit of waste reception <strong>and</strong> to one line of mechanical separation. Biofilters are made up of end compost.
208 Unit for Treatment of Air Emissions from the Composting Unit The unit consists of six (6) sub-units for the treatment of air emissions resulting from the composting process. The treatment is performed by employing chemical means; more specifically chemical scrubbing is performed. Each subunit is fed by one of the 6 main pipes that collect the air exhaust from the composting unit. Two sub-units correspond to one line from the composting unit. Each sub-unit consists of: One (1) tower for the removal of NH3 with the addition of Η2SO4. One (1) neutralization tower where NaOH is added One (1) tower for controlling the pH value <strong>and</strong> the Red/ox potential through the addition of hypochloric acid Six (6) chimneys Furthermore, the Ano-Liosia plant has supplementary facilities (e.g. fire fighting facilities, water <strong>and</strong> acid reservoirs etc), green installations, road facilities (e.g. roundabouts) <strong>and</strong> control buildings for most units. Each building is controlled through its Local Control Building. However, the whole operation of the facility is controlled from the Main Administration Building. (Morocomp.,2010) 11.4.2.The MBT plant in Chania The Solid Waste Recycling & Composting Plant (SWRC) <strong>and</strong> the Space for Sanitary Burial of Solid Waste (SSBSW) of the Prefecture of Chania was designed to collect <strong>and</strong> treat waste produced by the Municipalities of Chania, Akrotiri, Souda, Keramies, Eleftherios Venizelos, Therisos, Kydonia, Platania <strong>and</strong> Mousouri, although it has a much larger capacity. For that reason, it currently collects urban waste from the entire Prefecture of Chania, except for waste from Sfakia, Armeni, Pelekanos <strong>and</strong> Anatoliko Selino. The production of municipal solid waste by the Municipalities mentioned above is estimated to be 70,000 tons annually (based on the design) <strong>and</strong> the production of green waste is estimated to be 10,500 tons. 65% of the treated waste can be exploited as tradable recyclable <strong>and</strong> soil improvement material <strong>and</strong> the remaining 35% is buried in the SSBSW as residue.
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National Technical University of At
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3.3.4. Landfill sy
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10.4.2.Susteren sewage treatment <s
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Figure 44.: Västerås concept ....
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Picture 30.: The heat exchanger sys
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(Table 8.): The Ljungsjöverket pla
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2 1. Bio-WASTE MANAGEMENT LEGISLATI
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4 The Directive envisages the possi
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6 In the Commission's estimation, a
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8 of yard waste and</strong
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10 conditions (i.e., as brief as a
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12 Picture2.: View of machine used
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14 In-Vessel Composting Systems In
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16 The duration of the composting p
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18 Figure 7.: Principal emissions f
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20 2.2 Anaerobic Digestion (AD) 2.2
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22 4. Finally, methanogenic organis
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24 If the proper conditions cannot
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26 Considerations such as the desig
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28 to the viscosity of the feed, th
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30 The Netherlands
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32 Heavy metals in digestate usuall
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34 3. Large scale biodegradable was
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36 power and 1,200
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38 filtration or electrostatic prec
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40 acceptable range, but reduce the
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42 Rotary kiln furnaces Rotary kiln
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44 It has been processed an
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46 Heavy metals can be grouped into
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48 choices for a commercial plant w
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50 Gasification (Figure.19) using o
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52 AC plasma CO2 plasma arc Microwa
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54 pulled through an induced draft
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56 the non-biodegradables a
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58 3.3.8. Bioreactor land</
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60 4. Materials Sorting Processes 4
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62 Plastics Plastics (Fiqure.32) po
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64 separate containers. There are a
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66 The sorting of recyclables may b
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68 4.5. Mechanical and</str
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70 glass breakage on the tipping fl
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72 within solution under the influe
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74 material, and t
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76 changing pole configuration or w
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78 4.7. Mechanical Biological Treat
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80 Biological processing compartmen
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82 equivalence considerations <stro
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84 5.2. Waste streams considered in
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86 Figure 27.: Percentage of munici
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88 6.Italy The Italian strategy Ita
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90 Italy also set targets for colle
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92 (Figure 30.). The quality of com
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94 a controlled environment with wa
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96 Picture 11.: The Corteolona plan
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98 The building in the foreground h
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100 compost their garden waste. The
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102 The total amount of waste produ
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104 7. Germany 7.1. Waste managemen
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106 has been specified only for som
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108 7.3. Best practices</st
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110 The installation has different
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112 The sludge is placed into a lar
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114 Picture 22.: Air mixing mechani
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116 Finally the dried sludge is bee
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118 process treats the wastes as co
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120 consumption is about 0.7 x106 k
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122 Picture 30.: The heat exchanger
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124 used for the construction of l<
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126 International’. In the Drum D
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128 Picture 34.: Delivery crane in
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130 industrial processes, where <st
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132 industry, mixes the waste <stro
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134 8. Sweden The Swedish strategy
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136 joint committee or local govern
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138 upon the number of collected fr
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140 2004 2005 2006 2007 2008 Hazard
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142 Anaerobic digestion also produc
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144 Hässleholm 12,300 10,120 Karls
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146 distributed either through gas
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148 mentioned in earlier. (Chemical
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150 Picture 39.: Public fuelling st
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152 The pumpable organic waste is b
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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
Page 187 and 188: 176 Recycling Bins which are emptie
Page 189 and 190: 178 distance path. Since 1981, the
Page 191 and 192: 180 The scheme in operation in Wye
Page 193 and 194: 182 The method of composting the ga
Page 195 and 196: 184 such as: Waste, Management (of
Page 197 and 198: 186 heterogeneous in composition <s
Page 199 and 200: 188 2000 2004 2005 2006 Total 63,24
Page 201 and 202: 190 All domestic waste/recycling co
Page 203 and 204: 192 The end product is made into a
Page 205 and 206: 194 10.4.4. The Moerdijk incinerati
Page 207 and 208: 196 11. Greece The Greeks Strategy
Page 209 and 210: 198 The encouragement of rational o
Page 211 and 212: 200 Picture 55.: Panoramic View of
Page 213 and 214: 202 Four (4) ballistic separators
Page 215 and 216: 204 Picture 58.: View of Composting
Page 217: 206 Picture 59.: Refinery Unit at A
Page 221 and 222: 210 Picture 60.: Chania MBT plant (
Page 223 and 224: 212 A biological stabilization is t
Page 225 and 226: 214 Picture 66.: Prototype composti
Page 227 and 228: 216 Picture 69.: Psitallia sewage s
Page 229 and 230: 218 Figure 56.: Process description
Page 231 and 232: 220 Since ARTI-TZ started dissemina
Page 233 and 234: 222 Picture 74.: Construction of AD
Page 235 and 236: 224 biodegradables be isolated <str
Page 237 and 238: 226 Picture 77.: The physical separ
Page 239 and 240: 228 solution are fermented (e.g., s
Page 241 and 242: 230 Picture 78.: Transportation of
Page 243 and 244: 232 Picture 80.: Loofen company’s
Page 245 and 246: 234 The interior parts of both the
Page 247 and 248: 236 Figure 61.: Coway high capacity
Page 249 and 250: 238 13.3.1. Coway model (WM05-A) In
Page 251 and 252: 240 13.3.3. Coway model (WM03) The
Page 253 and 254: 242 13.5. DUO Enterprise Ltd Food g
Page 255 and 256: 244 References: Beyea, J., J. Cook,
Page 257 and 258: 246 Flaga A., 2003 Sludge Drying, I
Page 259 and 260: 248 Peigne, J., Girardin, P., 2004.
Page 261 and 262: 250 Internet sources: ACM Waste Man
Page 263 and 264: 252 Hellenic Statistical Authority.
Page 265 and 266: 254 Warwick District Council., 2010
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