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Malaysia - SETatWork - Sustainable Energy Technology at Work

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incentives from CDM will be 0.5 percent for 10 years of financial<br />

projection. However, with CDM financing, the IRR can be<br />

increased to 25 percent.<br />

A sensitivity analysis is conducted for another two other<br />

calcul<strong>at</strong>ions i.e. “reduced capital cost by 25 percent” and<br />

“increased value of energy production by 25 percent”. However,<br />

the sensitivity analysis shows th<strong>at</strong> the project IRR in all cases is<br />

un<strong>at</strong>tractive without the extra income from sale of CERs.<br />

5.5.3 Technical details:<br />

Technical<br />

details:<br />

The project will replace the existing open anaerobic systems<br />

(open digester tanks and lagoons) with well-proven closed,<br />

anaerobic contact digesters. This closed anaerobic digester<br />

technology is well-proven globally for managing high organic<br />

waste and commonly referred to as biogas or anaerobic digestion<br />

technologies.<br />

The POME will be distributed into the closed digesters <strong>at</strong><br />

appropri<strong>at</strong>ely spaced inlets <strong>at</strong> the bottom and flows to the top in<br />

an upward direction. The upward motion of the POME influent<br />

will improve the mixing in the digesters. The organic m<strong>at</strong>ters in<br />

the wastew<strong>at</strong>er are decomposed under anaerobic process. The<br />

decomposition process leads to the form<strong>at</strong>ion of biogas<br />

containing CH4 and CO2.<br />

The new anaerobic tank will be build from 10 mm mild steel with<br />

a stainless steel top cover pl<strong>at</strong>e. The existing tanks will get a 3<br />

mm steel pl<strong>at</strong>e enforcement to prevent leakage and a new<br />

stainless steel cover pl<strong>at</strong>e.<br />

In order to prevent gas leakage from the enclosed digester<br />

tanks, an overflow tank will be constructed. The overflow tank is<br />

the device where biogas and anaerobic liquor are separ<strong>at</strong>ed and<br />

the liquor can be discharged without escaping of the biogas.<br />

While the digested POME is channelled into aerobic ponds for<br />

further tre<strong>at</strong>ment, the captured biogas is pumped through a<br />

pipeline delivery system to the boiler for gener<strong>at</strong>ing steam.<br />

A new biomass boiler delivering 52 t steam/hour is being built to<br />

replace an existing biomass boiler. The new boiler is designed to<br />

fire a mix of biogas, palm kernel shells, mezocarp fibre and<br />

empty fruit bunches. The residence time of the biogas in the<br />

boiler is long compared to a gas engine solution and th<strong>at</strong> will<br />

secure th<strong>at</strong> the methane will be fully oxidised into CO2. The<br />

environmental performance of the new boiler will be better than<br />

the existing boiler and will live up to all environmental<br />

requirements. The boiler will be equipped with an autom<strong>at</strong>ed<br />

control system to improve performance and secure good<br />

combustion parameters <strong>at</strong> all times. The existing boiler is<br />

maintained for back up purposes.<br />

There is hardly any energy consumption of the project as it only<br />

includes pumping of the POME (which is also done in the<br />

baseline) and compression of the biogas before its is send to the<br />

boiler. The minimal project energy consumption is supplied from<br />

the biomass fired boiler and has thus no emissions of greenhouse<br />

36

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