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37<br />

<str<strong>on</strong>g>and</str<strong>on</strong>g> release of volatile substances from the combustible material, Igniti<strong>on</strong> <str<strong>on</strong>g>and</str<strong>on</strong>g><br />

oxidati<strong>on</strong> of volatile substances <str<strong>on</strong>g>and</str<strong>on</strong>g> finally combusti<strong>on</strong> of solid carb<strong>on</strong> in the<br />

presence of oxygen finishes the process. (B<strong>on</strong>toux.,1999)<br />

3.2.2.. Mass-burn incinerati<strong>on</strong><br />

During combusti<strong>on</strong> (Figure.14), the <strong>waste</strong> is burnt in the presence of a <str<strong>on</strong>g>good</str<strong>on</strong>g><br />

supply of air, so that <strong>organic</strong> carb<strong>on</strong> is essentially completely oxidized to<br />

CO2.In order for this process to be effective, the <strong>waste</strong> to be burnt is mixed well<br />

at the drying stage in order to dry properly. Al<strong>on</strong>g with water vapor <str<strong>on</strong>g>and</str<strong>on</strong>g> trace<br />

products of combusti<strong>on</strong>, CO2is discharged to the atmosphere. Energy is<br />

recovered in the form of steam, which is used to drive energy producti<strong>on</strong><br />

turbines for electricity generati<strong>on</strong> which is usually used for the incinerati<strong>on</strong><br />

plant energy c<strong>on</strong>sumpti<strong>on</strong>. Some incinerators may also provide steam or hot<br />

water for process or community heating schemes as well as electricity in<br />

combined heat <str<strong>on</strong>g>and</str<strong>on</strong>g> power (CHP) applicati<strong>on</strong>s. There are two main approaches<br />

to <strong>waste</strong> combusti<strong>on</strong> – mass-burn incinerati<strong>on</strong> <str<strong>on</strong>g>and</str<strong>on</strong>g> process <str<strong>on</strong>g>and</str<strong>on</strong>g> burn<br />

incinerati<strong>on</strong>, in which a refuse derived fuel (RDF) is first prepared.<br />

Mass-burn incinerati<strong>on</strong> (Figure 2.18) is currently the most widely deployed<br />

thermal treatment opti<strong>on</strong>, with almost 90% of incinerated <strong>waste</strong> being<br />

processed through such facilities. As the name implies, <strong>waste</strong> is combusted<br />

with little or no sorting or other pre-treatment. Waste arriving at a mass burn<br />

incinerator is tipped into a loading pit <str<strong>on</strong>g>and</str<strong>on</strong>g> from there after the drying process<br />

takes place usually at 75-80 o C (something that differs between different<br />

facilities), it is transferred by crane <str<strong>on</strong>g>and</str<strong>on</strong>g> grab system into the combusti<strong>on</strong><br />

chamber loading chute. The <strong>waste</strong> is then c<strong>on</strong>veyed through the combusti<strong>on</strong><br />

chamber, usually <strong>on</strong> a moving grate system (of which there are many designs)<br />

or through the slow rotati<strong>on</strong> of the combusti<strong>on</strong> chamber itself (rotary kilns).<br />

Whatever system is used, its purpose is to ensure thorough mixing, effective<br />

drying <str<strong>on</strong>g>and</str<strong>on</strong>g> even combusti<strong>on</strong> of the <strong>waste</strong>, so that complete burn-out has<br />

occurred by the time the ash residue is discharged into a water-filled quenching<br />

tank at the end of the combusti<strong>on</strong> chamber. Air is introduced from below <str<strong>on</strong>g>and</str<strong>on</strong>g><br />

above the grate at flow rates adjusted to suit the rate of combusti<strong>on</strong>.<br />

The hot combusti<strong>on</strong> gases pass through heat exchange secti<strong>on</strong>s of the<br />

combusti<strong>on</strong> chamber, where steam is generated for energy recovery. The<br />

cooling combusti<strong>on</strong> gases then pass through various stages of emissi<strong>on</strong> c<strong>on</strong>trol.<br />

These include dry or wet scrubbers for removing acid gases (SO, HCl), injecti<strong>on</strong><br />

of reducing agents such as amm<strong>on</strong>ia or urea for c<strong>on</strong>trolling NOx emissi<strong>on</strong>s,<br />

activated carb<strong>on</strong> injecti<strong>on</strong> for dioxin c<strong>on</strong>trol, <str<strong>on</strong>g>and</str<strong>on</strong>g> finally particulate removal by

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