(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 ...
39 conditions are achieved to prevent the formation of harmful products of incomplete combustion. Such conditions may occur when high quantities of wet garden waste come through the waste stream, especially in spring
40 acceptable range, but reduce the overall quantity of waste available for processing. Reduction in either the calorific value or quantity of waste consumed would reduce the amount of energy recovered, the sale of which provides one of the main income streams (along with the disposal fee) of the incinerator. Reductions in the sales value of energy would then feed through into higher disposal charges for the waste. 3.2.3. Types of incinerators There are various types of incinerators (Figure.15): Moving grate, fixed grate, rotary-kiln, fluidized bed, etc (Fig.). Figure 15. : Three types of incinerators: (a) fixed grate (left), (b) rotary kiln (middle), (c) fluidized bed (right) (Solid Waste Management through the Application of Thermal Methods.,2010) Grate furnaces Grate furnace incinerators (Figure 16.) are by far the most common technology for the incineration of MSW. They perform the so-called mass burn which requires minimal pre-processing (such as sizing, shredding, etc.)
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39<br />
c<strong>on</strong>diti<strong>on</strong>s are achieved to prevent the formati<strong>on</strong> of harmful products of<br />
incomplete combusti<strong>on</strong>. Such c<strong>on</strong>diti<strong>on</strong>s may occur when high quantities of<br />
wet garden <strong>waste</strong> come through the <strong>waste</strong> stream, especially in spring <str<strong>on</strong>g>and</str<strong>on</strong>g><br />
autumn.<br />
Several material streams emerge from mass-burn incinerati<strong>on</strong>. The greatest of<br />
these is the ash residue discharged from the combusti<strong>on</strong> chamber, which may<br />
represent between 20 – 30% of the mass of <strong>waste</strong> c<strong>on</strong>sumed. The ash may be<br />
processed by stabilizing <str<strong>on</strong>g>and</str<strong>on</strong>g> grading to form a useful sec<strong>on</strong>dary c<strong>on</strong>structi<strong>on</strong><br />
material that can be used for low-grade applicati<strong>on</strong>s such as road or car-park<br />
base layers. Re-use of incinerator ash varies from country to country. Most of<br />
the existing incinerators in the UK <str<strong>on</strong>g>and</str<strong>on</strong>g> all plants in the Netherl<str<strong>on</strong>g>and</str<strong>on</strong>g>s have an<br />
ash processing facility. Ash which cannot be re-used is l<str<strong>on</strong>g>and</str<strong>on</strong>g>filled. Metals can<br />
also be recovered from the bottom ash <str<strong>on</strong>g>and</str<strong>on</strong>g> sold to preprocessors. In plants with<br />
an ash-processing facility, nearly all of the ferrous metal can be recovered;<br />
otherwise up to 90% can be recovered. N<strong>on</strong>-ferrous metal can also be recovered<br />
in plants with ash processing.<br />
Emissi<strong>on</strong>s st<str<strong>on</strong>g>and</str<strong>on</strong>g>ards for incinerators have recently been tightened through new<br />
emissi<strong>on</strong> limits imposed under the new incinerati<strong>on</strong> directive <str<strong>on</strong>g>and</str<strong>on</strong>g> extensive<br />
treatment of the flue gases is necessary to meet the new limits. Residue is<br />
produced from the air polluti<strong>on</strong> c<strong>on</strong>trol system, representing about 2-4% by<br />
weight of the incoming <strong>waste</strong>.<br />
This material c<strong>on</strong>sists of salts <str<strong>on</strong>g>and</str<strong>on</strong>g> surplus alkali from acid gas neutralizati<strong>on</strong>;<br />
although some plants using wet scrubber systems currently discharge the<br />
scrubber residues to water as a salts soluti<strong>on</strong>. In additi<strong>on</strong>, fly ash c<strong>on</strong>taining<br />
dioxin <str<strong>on</strong>g>and</str<strong>on</strong>g> heavy metals is produced. This material requires disposal at<br />
hazardous <strong>waste</strong> l<str<strong>on</strong>g>and</str<strong>on</strong>g>fills, usually after some form of stabilizati<strong>on</strong> or<br />
immobilizati<strong>on</strong> in an inert medium such as cement has taken place. In<br />
Germany, salt caverns are used for storage of such hazardous materials.<br />
To be cost-effective, mass burn incinerators require a guaranteed supply of<br />
<strong>waste</strong> within known limits of compositi<strong>on</strong>, available throughout the life of the<br />
plant. Because of the large scale of operati<strong>on</strong>, such facilities may effectively<br />
‘lock-in’ supplies of <strong>waste</strong> that could otherwise go for recycling. In additi<strong>on</strong>,<br />
the requirement for bulk <strong>waste</strong> to be provided within a relatively narrow range<br />
of calorific value means that removal of particular <strong>waste</strong> streams for recycling<br />
could cause the remaining <strong>waste</strong> to fall outside the acceptable range.<br />
For example, removal of paper <str<strong>on</strong>g>and</str<strong>on</strong>g> / or plastics for recycling would increase the<br />
relative proporti<strong>on</strong> of putrescible <strong>waste</strong> in the residue <str<strong>on</strong>g>and</str<strong>on</strong>g> lower its calorific<br />
value. On the other h<str<strong>on</strong>g>and</str<strong>on</strong>g>, removal of putrescible <strong>waste</strong>s as well, for<br />
composting, would help to keep the calorific value of the residue in the