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

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1007<br />

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

€3.08 under the high externalities (mostly from the use <strong>of</strong> diesel);<br />

2. Total direct emissions from the stabilisation process and the landfilling <strong>of</strong> the<br />

residues result in external damage costs <strong>of</strong> €0.47 under the high externalities<br />

(emissions <strong>of</strong> NMVOCs from stabilisation account for most <strong>of</strong> this impact).<br />

63.5 MBT Aerobic Biodrying Systems<br />

63.5.1 Climate Change Impacts <strong>of</strong> MBT Aerobic Biodrying Systems<br />

Biodrying systems involve the application <strong>of</strong> intensive heat to the waste to ensure the<br />

removal <strong>of</strong> moisture prior to it being used as fuel. During this process degradation <strong>of</strong><br />

some <strong>of</strong> the carbon fractions will occur as a result <strong>of</strong> the increase in temperature but<br />

the amount <strong>of</strong> degradation is relatively limited in comparison that occurring during<br />

aerobic decomposition (stabilisation) processes.<br />

Emissions <strong>of</strong> CO2 are calculated from the carbon loss estimated over a two week<br />

period. The figures for carbon loss are estimated by ourselves for each <strong>of</strong> the<br />

components <strong>of</strong> the waste stream. We have been able to correlate these estimates<br />

over several years using an analysis <strong>of</strong> data from technology suppliers.<br />

The central aim <strong>of</strong> biodrying processes is to produce a fuel. A reject stream is also<br />

produced, which is assumed to be stabilised before being sent to landfill, using the<br />

process previously described in Section 0.<br />

Table 63-15 outlines key assumptions used to model the biodrying phase.<br />

Our assumptions regarding the nature <strong>of</strong> the SRF produced are detailed in Table<br />

63-16.<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 />

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

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