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International Review of Waste Management Policy - Department of ...

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1009<br />

� Optimised bi<strong>of</strong>ilter; and<br />

� Thermal filter.<br />

The choice <strong>of</strong> abatement equipment determines the level <strong>of</strong> removal <strong>of</strong> some <strong>of</strong> the<br />

gases prior to their emission to the atmosphere. It also determines the level <strong>of</strong> energy<br />

use in the process (especially relevant for the thermal filter option).<br />

We have assumed that MBT facilities operate with optimised bi<strong>of</strong>ilters. The<br />

requirement, in Germany, to deploy regenerative thermal oxidation (or other)<br />

processes to crack remaining VOCs from the exhaust gas appears, in our view, to be<br />

unjustifiable when the additional benefits are set against the additional energy<br />

demand implied by the process. 1252<br />

Pollution abatement techniques employed at incineration facilities have been<br />

previously discussed in Section 63.3.2. Again we have assumed two types <strong>of</strong> facilities<br />

– one which complies with the WID, and a second which has installed additional<br />

abatement equipment and therefore exceeds the requirements <strong>of</strong> the WID. Our<br />

assumptions for the landfill <strong>of</strong> pre-treated (stabilised) material have been previously<br />

discussed in Section 63.2.1.5.<br />

Our analysis considers two uses for the output from the biodrying process:<br />

1. The SRF is combusted at a dedicated incineration facility generating electricity<br />

as has been previously described in Section 63.3.<br />

2. The SRF is combusted at a cement kiln where it is assumed to displace the<br />

use <strong>of</strong> coal. We assume a 90% substitution ratio for the fuel displacement,<br />

and that the coal would otherwise emit 0.37 kg CO2 equivalent per kWh <strong>of</strong><br />

energy generated.<br />

Our assumptions for the landfill <strong>of</strong> pre-treated (stabilised) material have been<br />

previously discussed in Section 63.2.1.5.<br />

The principal air quality impacts are:<br />

1. Energy used within the treatment process, giving rise to damage costs <strong>of</strong><br />

€6.42 under high externalities or €2.22 assuming low external costs. Most <strong>of</strong><br />

this impact arises from the use <strong>of</strong> diesel within the facility. 1253<br />

2. Where the SRF is sent to an incinerator, total emissions from direct treatment<br />

processes (including the biodrying and stabilisation components and the<br />

combustion <strong>of</strong> SRF as well as the landfilling <strong>of</strong> residues) result in external<br />

damage costs <strong>of</strong> €10.64 under the higher externalities or €3.69 assuming low<br />

1252 Bi<strong>of</strong>ilters themselves are sources <strong>of</strong> VOCs, though typically <strong>of</strong> less benign species than the type<br />

one seeks to remove from exhaust gases. To assume that all VOCs are equally detrimental to air<br />

quality and health is to misunderstand the problem, and although RTO deployment will further reduce<br />

VOC emissions, (as we show within this review) it tends to do so at considerable additional cost from<br />

the perspective <strong>of</strong> climate change.<br />

1253 The additional diesel consumption reflects that used within the incineration <strong>of</strong> SRF. Assumptions<br />

used here are the same (on a per tonne basis) as for the incineration <strong>of</strong> untreated wastes.<br />

<strong>International</strong> <strong>Review</strong> <strong>of</strong> <strong>Waste</strong> <strong>Policy</strong>: Annexes

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