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Summary<br />

In order to demonstrate a reduction of methane emissions, a Smell-Well system was installed<br />

and operated on a part of the slope of the Braamberg<strong>en</strong> landfill near Almere, the Netherlands in<br />

the period of October 2000 until August 2002. In the Smell-Well system alternately air is<br />

injected or extracted through a relative large number of lances, located about 5 meters away<br />

from each other.<br />

Air injection might have a number of effects:<br />

(i) the existing capacity for methane oxidation in the top-layer can be <strong>en</strong>hanced;<br />

(ii) further methane formation in the aerobic part of the landfill is prev<strong>en</strong>ted, since traces of<br />

oxyg<strong>en</strong> are toxic for the methanog<strong>en</strong>s responsible for methane g<strong>en</strong>eration;<br />

(iii) in pres<strong>en</strong>ce of suffici<strong>en</strong>t oxyg<strong>en</strong>, organic material will decompose aerobically and the<br />

pot<strong>en</strong>tial for methane formation is removed;<br />

(iv) the d<strong>en</strong>se system of lances will act as an effici<strong>en</strong>t system for surface extraction of<br />

landfill gas, migrating through the top-layer.<br />

The demonstration is int<strong>en</strong>sively monitored; methane emissions are measured, the quality of<br />

pore water is analyzed and waste samples are tak<strong>en</strong> and analyzed prior to and after aeration.<br />

Besides the process of aerobic conversion is <strong>en</strong>hanced on a lab-scale in order to be able to<br />

study the possibility of an aerobic landfill, in which the waste is composted in-situ.<br />

Main conclusion is that Smell-Well reduces methane emissions with 60-85%. In the<br />

demonstration from January 2001 until May 2001 the emission of 580.000 Nm 3 of methane was<br />

reduced; wh<strong>en</strong> the system is continued and operates without any major problems, an average<br />

annual emission reduction can be expected of about 500.000 Nm 3 of methane (0.36 ktonne<br />

CH4 y -1 ; 7.6 ktonne CO2-equival<strong>en</strong>ts y -1 ). The most important mechanism is mechanism (iv): an<br />

effici<strong>en</strong>t surface extraction of the gas. Besides it is demonstrated that mechanism (i), a<br />

stimulation of methane oxidation is also of importance. The extra methane oxidation due to<br />

Smell-Well is 13-23% of total methane flux through the top layer.<br />

Investm<strong>en</strong>ts were € 1.14 million, and annual operating costs are € 70.000. The costs for<br />

gre<strong>en</strong>house gas mitigation were € 27 per tonne CO2-equival<strong>en</strong>ts, which is quite exp<strong>en</strong>sive. On<br />

the basis of insights gathered in this study, a simplified system can be designed, costing about<br />

€ 6 per tonne CO2-equival<strong>en</strong>ts.<br />

With regards to the feasibility of aerobic landfills, the full-scale and lab-scale experim<strong>en</strong>ts led to<br />

contradictions:<br />

on a full-scale, aerobic conversion of organic material could not be prov<strong>en</strong> to have<br />

occurred;<br />

on a lab-scale aerobic stabilization proceeded rather fast and the organic material was<br />

completely stabilized within about half a year.<br />

On the basis of these results, no conclusions can be drawn about the technical feasibility of<br />

aerobic landfills. One conclusion that can be drawn is that the pres<strong>en</strong>ce of an d<strong>en</strong>se system for<br />

aeration is no guarantee for swift aerobic stabilization. Additional monitoring of methane<br />

emissions and waste conversion are required in order to demonstrate the feasibility of an<br />

aerobic landfill.<br />

On the full-scale an improvem<strong>en</strong>t of pore-leachate is observed. A comparison of fully aerobic<br />

stabilized waste, anaerobically stabilized organic waste and largely inorganic waste showed<br />

3

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